4
T. Ishida et al. / Tetrahedron xxx (2014) 1e6
(
Pd/CMP-OH). The Pd/CMP-OH was prepared from 1,3,5-
triethynylbenzene and 1,4-dihydroxy-2,5-diiodobenzene, fol-
lowed by the H treatment to give Pd/CMP-OH-H . The mean di-
ameter of Pd NPs of Pd/CMP-OH-H was estimated to be
Table 3
a
Hydrogenation of 4-nitrostyrene
2
2
2
3
.9ꢂ0.9 nm by HAADF-STEM (Fig. S8).
Entry
Catalyst
Conv.b (%)
4b (%)
5b (%)
6b (%)
1
2
3
Pd/CMP-1
Pd/CMP-1-H
Pd/KB
4
>99
>99
>99
0
>99
0
0
0
0
0
0
0
93
56
2
.2. Pd/CMP-catalyzed hydrogenation
2
c
Catalytic performance of Pd/CMP-1-N
2
and -H
2
was examined
4
Pd/KB
42
using hydrogenation of N-benzylideneaniline as a model reaction
a
4
-Nitrostyrene (0.5 mmol), Pd cat. (Pd 1 mol %), dehydrated toluene (3 mL), H
2
(
(
Table 2). For the comparison, Pd NPs supported on Ketjen black
KB), which has similar BET surface area (700 m /g), was used. N-
ꢀ
(
0.3 MPa), 50 C, 1 h.
2
b
Calculated on the basis of GC analysis using anisole as an internal standard.
H (0.1 MPa), rt, 30 min.
2
c
Benzylideneaniline was converted into N-benzylaniline (1) over
Pd/CMP-1, whereas the hydrolysis of imine also proceeded to give
aniline and benzaldehyde as major products due to the presence
of a trace amount of H O (entry 1). When Pd NPs were formed in
2
the CMP framework, the catalytic performance was remarkably
et al. have reported that zeolite (MS-3A and MS-5A) supported Pd
NPs showed selectivity to olefin, and they catalyzed the hydroge-
nation of 4-nitrostyrene to give 4-ethylnitrobenzene (4) with ex-
improved, and N-benzylaniline was obtained as a major product
13
2
cellent selectivity. Pd/CMP-1-H also showed excellent selectivity
(
entries 2 and 3). Moreover, Pd/CMP-1-H
NPs, exhibited higher catalytic activity and selectivity than Pd/
CMP-1-N did. It is likely that terrace Pd atoms work as active
2
, which has larger Pd
to 4 (entry 2), whereas the complete hydrogenation of 4-
nitrostyrene to 4-ethylaniline (6) could not be suppressed over
Pd/KB even under mild reaction conditions (entry 4). Baiker et al.
have reported that the chemoselectivity for the 3-nitrostyrene
hydrogenation could be controlled by reaction media. In their
report, CeC double bond was preferentially hydrogenated in acidic
media. Taking into account the fact, acidic sites of supports would
play an important role for Pd-catalyzed selective hydrogenation.
Interestingly, Pd/CMP-1-H exhibited olefin selectivity, although
2
CMP framework has neither acidic nor basic sites.
Although the catalytic performance of Pd/CMP-OH-H
alter from Pd/CMP-1-H
neaniline (Table 2, entry 7), Pd/CMP-OH-H
lytic activity than Pd/CMP-1-H for the oxidation of benzyl alcohol
Table 4). Pd/CMP-1-H slightly improved the benzaldehyde yields
from Pd/CMP-1 (entries 1 and 2). In contrast, Pd/CMP-OH-H re-
2
sites, as previously observed in the Pd NP-catalyzed alkene hy-
drogenation, in which terrace Pd atoms showed higher catalytic
14
activity than edge and corner Pd atoms did.11b,12 Another possi-
bility is ascribed to the removal of phosphine ligands from the
surface Pd atoms by H
atoms, which can dissociate H
2
treatment, giving the bare surface Pd
. Hexane was more beneficial sol-
2
vent and N-benzylaniline could be obtained in 87% yield (entry 4).
Pd/KB also catalyzed the hydrogenation, but the hydrogenolysis of
2
did not
1
to toluene and/or the reduction of benzaldehyde to benzyl al-
2
for the hydrogenation of N-benzylide-
cohol and the further hydrogenolysis of benzyl alcohol to toluene
also occurred (entry 5). Inductively coupled plasma atomic emis-
sion spectroscopy (ICP-AES) analysis proved that leaching Pd into
the reaction solution was below detection limit (<0.1 ppm) for Pd/
CMP-1-H , whereas 5.3% Pd from the initial Pd loading leached
2
into the reaction solution for Pd/KB. From these results, CMP
frameworks appeared to be effective supports for metal clusters.
2
exhibited higher cata-
2
(
2
2
markably improved the catalytic activity from that of Pd/CMP-OH,
and gave benzaldehyde in 73% yield, which was even higher than
that for Pd/CMP-1-H (entry 4). It is likely that hydroxy groups in
2
Pd/CMP-2-H
2
2
and Pd/CMP-OH-H showed similar catalytic activity
the CMP framework affected the catalytic activity of Pd NPs.
to that of Pd/CMP-1-H
2
(entries 6 and 7), probably due to the
similar or smaller size of Pd NPs.
Table 4
a
Oxidation of benzyl alcohol
Table 2
a
Hydrogenation of N-benzylideneaniline
Entry
Catalyst
Conv.b (%)
Benzaldehydeb (%)
1
2
3
4
Pd/CMP-1
Pd/CMP-1-H
Pd/CMP-OH
37
35
42
74
20
34
27
73
2
Entry
Catalyst
Conv.b (%)
1b (%)
2b (%)
3b (%)
Pd/CMP-OH-H
2
1
2
3
4
5
Pd/CMP-1
23
57
79
4
32
72
87
57
77
73
14
21
5
3
31
5
15
19
4
2
0
a
Benzyl alcohol (0.25 mmol), Pd cat. (Pd 2 mol%), dehydrated toluene (3 mL), O
2
Pd/CMP-1-N
Pd/CMP-1-H
Pd/CMP-1-H
Pd/KB
Pd/CMP-2-H
Pd/CMP-OH-H
2
2
2
ꢀ
(
1.0 MPa), 150 C, 4 h.
b
Calculated on the basis of GC analysis using dodecane as an internal standard.
c
91
d
>99
>99
82
e
6
7
2
Trace
8
3. Conclusions
2
8
a
N-Benzylideneaniline (0.5 mmol), Pd cat. (Pd 1 mol %), dehydrated toluene
ꢀ
2
3 mL), H (0.5 MPa), 100 C, 4 h.
In summary, we have prepared the Pd NPs encapsulated by
microporous polymer networks, CMPs, by the Pd-catalyzed poly-
merization followed by thermal treatment. The Pd catalysts were
fixed in the CMP porous structures during the polymerization and
aggregated to form Pd NPs by the thermal treatment. Palladium NPs
were highly dispersed in the porous structures, even though CMP
frameworks had no interaction sites with Pd. Once Pd NPs were
formed, the catalytic activity was significantly improved for hy-
(
b
Calculated on the basis of GC analysis using dodecane as an internal standard.
Hexane (3 mL) was used instead of toluene.
c
d
e
1
H
h.
2
(1.5 MPa), 5 h.
2
The catalytic performance of Pd/CMP-1-H was further exam-
ined by the hydrogenation of 4-nitrostyrene and results are shown
in Table 3. Heterogeneous Pd NP-catalyzed selective hydrogena-
tions of alkenes in the presence of nitro groups are limited. Sajiki
drogenations and oxidations. In addition, Pd/CMP-1-H was active
2
for the selective hydrogenation of 4-nitrostyrene into 4-