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a
Table 1 Selective oxidation of styrene catalyzed by McaILs/PdCl2
Entry
IL
IL/Pd (mol/mol)
TOFd/hÀ1
C (%)
S (%)
1
2
3
4
5
6
a
3bb
—
3b
3d
4b
5b
—
0
1.1
2.0
1.4
2.3
—
21
146
125
116
92
8
25
100
100
84
7
86
93
91
92
92
c
80
Reaction conditions: reaction was carried out in a 250 mL round-
bottomed flask fitted with a condenser; styrene (250 mmol, 26.03 g),
30% H2O2 (287.5 mmol, 32.59 g), PdCl2 (0.25 mmol, 0.0446 g),
b
c
temperature = 55 1C. Without PdCl2, 8 h. Without McaIL,
8 h. TOF: turnover frequency: number of moles of styrene converted
d
per mole of palladium catalyst per hour. C (%): conversion of styrene;
S (%): selectivity of acetophenone.
Fig. 1 Effect of temperature on the oxidation of styrene with H2O2 in
the presence of 3b/PdCl2: selectivity of acetophenone (B), selectivity of
benzaldehyde (n), conversion (K) and TOF value (&). Reaction
conditions: reactions were carried out in a 250 mL round-bottomed
flask fitted with a condenser until the conversion of styrene maintained
invarient; styrene (250 mmol, 26.03 g), 30% H2O2 (287.5 mmol,
32.59 g), PdCl2 (0.25 mmol, 0.0446 g), 3b : PdCl2 = 1.1 : 1.0; TOF:
turnover frequency, number of moles of styrene converted per mole of
palladium catalyst per hour; C (%): conversion of styrene; S (%):
selectivity of acetophenone.
ESI-MS (for 3b and 5b) and 168 (for 4b) representing
the presence of [PdCl4]2À , [PdCl2Br2]2À
1
2
(
m/z due to the
À2 charge).
Using the ionic acid 3b and PdCl2, the optimal temperature
was found at 55 1C (Fig. 1), under which conditions
the conversion of styrene was virtually 100% within 7 h of
reaction time and the measured TOF value (146 hÀ1) was
six times higher than that of PdCl2 catalyst. Furthermore, the
selectivity of acetophenone was as high as 93%. For
all McaIL/PdCl2 catalyst systems, with the increase of
molar ratio of McaIL to PdCl2, the selectivity of acetophenone
increased, however, it was found that the conversions
of styrene and the TOF values peaked at a certain molar
ratio, which was different in different McaIL systems. For
example, using the same cation the optimized molar ratio for
3b to PdCl2 was 1.1 (entry 3), 2.0 for 3d (entry 4) while the
optimized molar ratio for 3b, 5b with ClÀ anion and 4b with
BrÀ to PdCl2 was 1.1 (entry 3), 2.3 (entry 6) and 1.4 (entry 5),
respectively.
acid, which is always the by-production of the selective
oxidation of styrene, cannot be detected upon any McaIL/
PdCl2 samples, implying that McaILs/PdCl2 could inhibit the
generation of deep oxidation products of styrene. This could
be rationalised in that the deep oxidation products are sup-
pressed as the transition process of the intermediate transient
state is prevented to form carboxylic groups by these carboxyl
groups present in the McaIL/PdCl2 systems. Further study
on the detailed catalytic mechanism of McaILs/PdCl2 is on-
going in our laboratory and the results will be communicated
elsewhere.
Other acids with BF4À, PF6À, CF3COOÀ and CF3SO3
To illustrate the advantage of the McaIL/PdCl2 catalytic
systems we compared our McaILs/PdCl2 with C4mimBF4/
PdCl2, C4mimPF6/PdCl2, oxalic acid/PdCl2, succinic acid/
PdCl2 and acetic acid/PdCl2 systems. For the C4mimBF4/
PdCl2 and C4mimPF6/PdCl2 systems we achieved similar
results as those reported in the literature with the selectivity
of acetophenone being slightly lower.26 In the presence of
palladium chloride, these neutral carboxylic acid–PdCl2
systems could catalyze the oxidation of styrene but they all
gave consistently lower conversions (28–46%) with lower
selectivity towards acetophenone (73–84%).
À
anions gave slightly lower conversions than 3b/PdCl2,
4b/PdCl2 and 5b/PdCl2. In most cases, the conversion can
reach as high as 90%, but the selectivity to the side-product
benzaldehyde was significantly increased (2–23%) at the ex-
pense of acetophenone. Anion effects have been observed in
other catalytic systems where the anions of the ionic liquids
played a major role in the catalytic performance.24 As in this
case, the reduced activity of 3d–3g, 4d–4g and 5d–5g/PdCl2
systems could be attributed to the interaction(s) between
palladium chloride and the McaILs. In contrast to the ILs
3b, 4b and 5b, ILs 3d–3g, 4d–4g and 5d–5g did not form a
homogeneous solution upon addition of PdCl2. The suspen-
sions obtained instead can be partially dissolved upon heating
the mixture to 55 1C. The solids, isolated from the suspension
through centrifugation, all showed an absorption at 1650 cmÀ1
in the IR spectra, a remarkable shift compared to the absorp-
tion value of the corresponding free acid (1720 cmÀ1), which
strongly indicates a coordination of Pd ion with carboxylic
groups as (COO–Pd).25 Though the coordination mode the
carboxylic groups to the palladium could be complicated, we
believe, due to the presence of the multi-carboxylic groups,
formation of polymeric structures is possible. Phenylformic
A further major advantage of using McaILs was reflected in
their facile separation and recycling with the palladium
catalyst. After distillation of the reaction mixture,27 the
impurities formed during the oxidation process can all be
removed by washing the McaIL–palladium containing
mixture with cold acetone. Due to the low solubility of the
McaILs, most of the McaILs/Pd can be recovered. In our
previous paper, the susceptibility of dialkylimidazolium ionic
liquids to oxidative degradation under oxidizing conditions
was reported,28 but it should be mentioned here that the
oxidation of McaILs could not be observed in the present
work. Thus, the obtained McaIL/PdCl2 mixtures can be
ꢀc
This journal is the Royal Society of Chemistry and the Centre National de la Recherche Scientifique 2007
New J. Chem., 2007, 31, 2088–2094 | 2091