C. Liu et al. / Tetrahedron Letters 56 (2015) 6460–6462
6461
Table 1
were chemoselectively hydrogenated into aminobenzylamines.
The hydrogenations of 1a catalyzed by the Pd/Ni bimetallic catalysta
Since the Pd/Ni ratio was about 1:99 (by wt %), we hypothesized
that most or all of the Pd-atoms on the surface of this catalyst were
surround by Ni-atoms to form the heterometallic Pd–Ni bonds.
Unlike the Pd–Pd and Ni–Ni bonds, Pd–Ni bond is a polarized bond
that may be described as dÀPd–Nid+ (electronic effect or ligand
effect), by which the Pd/Ni bimetallic catalyst demonstrated novel
catalytic ability and chemoselectivity that differ from their parent
metals.10 As shown in Scheme 2, the polarized Pd/Ni bimetallic cat-
alyst may have stronger adsorptivity for the heteroatom double
bond than for the heteroatom single bond. This hypothesis also
strongly implied that the EDG-substituted benzaldehydes 1 (with
heteroatom double bond) may be chemoselectively hydrogenated
into the corresponding benzyl alcohols 2 (with heteroatom single
bond) by using the same catalyst.
1% Pd/Ni, H2
MeOH, rt, time
71-98% yield
100% chemoselectivity
MeO
MeO
MeO
MeO
OH
O
OMe
1a
OMe
2a
Entry
1% Pd/Ni (wt %)
Timeb (h)
Pressure (psi)
Yield of 2ac (%)
1
2
3
4
100
50
30
20
20
10
10
1.5
2.5
3.5
6.5
6.0
6.0
6.0
—
—
—
—
30
30
60
94
97
98
91d
98
5e
6e
7e
71d
96
To prove our hypothesis, 3,4,5-trimethoxybenzylaldehyde (1a)
was used as a model substrate because its hydrogenation product
3,4,5-trimethoxybenzyl alcohol (2a) is highly sensitive to further
catalytic hydrogenolysis. As shown in Scheme 3, five commercial
Pd-catalysts A–E were initially tested on the hydrogenated of 1a
and three products 2a, 3a and 4a were detected with variable
ratios. But, none of them gave an acceptable hydrogenation
chemoselectivity.
a
A mixture of 1a (196 mg, 1 mmol) and the Pd/Ni bimetallic catalyst in MeOH
(10 mL) was stirred under H2 at room temperature (on an atmospheric pressure
hydrogenation apparatus).
b
The time was when the absorption of hydrogen ceased.
Separated yield was obtained.
Only the unreacted substrate 1a was recovered.
The experiments proceeded on a Parr-hydrogenator.
c
d
e
As was expected, the hydrogenation of 1a gave 2a as a unique
product over the Pd/Ni bimetallic catalyst. As shown in
Table 1, 2a was obtained in 94% yield and 100% chemoselectivity
under the conditions listed in entry 1. Since the net weight of pal-
ladium metal used in this entry was much more than that used in
Scheme 3, the chemoselectivity must arise from the synergistic
effects of the Pd/Ni bimetallic catalyst. The quantitative yield and
chemoselectivity of 2a were obtained when 30 wt % Pd/Ni bimetal-
lic catalysts were used (entry 3). Although 2a was obtained in
lower yield (91%) by use of 20 wt % Pd/Ni bimetallic catalysts, its
chemoselectivity was not affected (entry 4). When the hydrogena-
tion was operated on a Parr-hydrogenator by slightly increasing
the hydrogen pressure, 10 wt % Pd/Ni bimetallic catalysts were
good enough to produce excellent results (entries 5–7).
The conditional experiments for reaction solvents and recycling
studies of the Pd/Ni bimetallic catalyst gave very similar results to
those reported in our previous work.9 For example, MeOH was the
best solvent for this hydrogenation and the catalytic activity of the
catalyst decreased sharply after four recycles. Thus, the standard
1% Pd/Ni (30 wt%), H2 (atm)
previous work
NR2
NR2
OH
MeOH, rt, 3.5-5.3 h
96-98% yields
100% chemoselectivity
OH
OH
O
EDG
EDG
O2N
H2N
Pd/Ni, H2 (atm), MeOH, rt
1a-1t
2a-2t
?
O
EDG
EDG
MeO
MeO
proposed work
OH
OH
OH
1
2
MeO
EtO
EtO
OMe
OMe
OMe
OEt
Scheme 2. Proposed chemoselective hydrogenation.
2a (3.5 h, 98%)
2b (4.1 h, 98%)
2c (4.0 h, 98%)
2d (4.0 h, 97%)
HO
O
OH
Me2N
OH
HO
2g (5.5 h, 98%)
OH
OH
MeO
catalysts A-E (5 wt%), H2 (atm), MeOH, rt, 3.5 h
the ratios of 2a:3a:4a
O
O
MeO
were determined by 1H NMR spectra
2e (4.0 h, 97%)
2f (4.0 h, 97%)
2h (5.3 h, 98%)
1a
OMe
MeO
OH
OH
OH
OH
MeO
MeO
MeO
MeO
Me
MeO
MeO
OH
OMe
+
+
MeO
2j (4.5 h, 98%)
OH
OMe
2l (3.5 h, 98%)
2i (5.3 h, 97%)
2k (4.7 h, 98%)
PhO
OMe
2a
71%
0%
33%
13%
0%
OMe
3a
OMe
4a
0%
58%
0%
0%
0%
F3CO
OH
OH
OH
OH
OH
Cat-A
Cat-B
Cat-C
Cat-D
Cat-E
29%
42%
PrnO
BnO
67%
2m (4.1 h, 97%)
2n (4.0 h, 97%)
2o (4.3 h, 99%)
2p (5.0 h, 98%)
87%
100%
Me
Scheme 3. Hydrogenations over five commercial Pd-catalysts. Cat-A: Acros-
199620100, palladium hydroxide on carbon powder, 20% Pd. Cat-B: Aldrich-
330108, palladium, 10 wt % on activated carbon. Cat-C: Alfa Acesar-A26D10,
palladium, 5 wt % on activated carbon powder, unreduced. Cat-D: Alfa Acesar-
K08P30, palladium, 5 wt % on activated carbon powder, reduced, acidic catalyst.
Cat-E: Shanxi Kaida product, palladium, 10 wt % on activated carbon powder.
OH
OH
OH
Me
2s (5.0 h, 98%)
Me
2q (4.5 h, 96%)
2r (4.7 h, 97%)
2t (5.0 h, 96%)
Scheme 4. The scope of the hydrogenation.