6
C. Lou et al. / Catalysis Communications 90 (2017) 5–9
magnetically stirred at 353 K in oil bath for 6 h with O
product analysis was performed by GC using the internal standard
method. Control experiments including using Pd(OAc)
alone were carried out in parallel.
2
balloon. The
experiments using Lewis acid as catalyst demonstrated ignorable activ-
ity for dehydrogenation, thus eliminated the role of impurities in
dehydrogenation.
2 2
, or Zn(OTf)
The influence of Zn(II)/Pd(II) ratio on indoline dehydrogenation was
2 2
displayed in Fig. S2. Increasing the ratio of Zn(OTf) /Pd(OAc) up to 4
3
. Results and discussion
still continuously improved the dehydrogenation efficiency, which is
similar to that in Lewis acid promoted Wacker-type oxidation by
To screen the Lewis acid for the Pd(OAc)
2
catalyzed dehydrogena-
2
Pd(OAc) catalyst, but different from that in olefin isomerization [15,
tion, an easy substrate, indoline, was first tested for aerobic oxidative
dehydrogenation, and the reactions were conducted in acetonitrile
17]. In olefin isomerization, increasing the ratio of Al(III)/Pd(II) from 0
to 1 can sharply improve the isomerization efficiency, while further in-
creasing the ratio does not show significant improvement. Catalytic ki-
netics of 2-methylindoline dehydrogenation also disclosed that adding
with O
2
balloon at 353 K with stirring. The results are listed in Table 1.
alone can offer
8.7% conversion of indoline with 34.3% yield of indole. Without
One may see that, in the control experiment, Pd(OAc)
3
2
2 2
Zn(OTf) displays a clear faster reaction rate than using Pd(OAc)
Pd(OAc)
2
, exposing indoline to the reaction conditions also provided
alone. As shown in Fig. 1, Lewis acid alone as catalyst shows the identical
dehydrogenation rate as that of no catalyst added, supporting that
1
3.2% conversion with 10.8% yield of indole due to its instability. Adding
NaOTf to Pd(OAc) did not improve its dehydrogenation efficiency,
while adding 2 equiv. of bivalent metal ions like Ca , Mg , and
2
Zn(OTf)
Pd(OAc)
2
alone cannot catalyze the reaction. Without Lewis acid,
alone is active but the dehydrogenation rate is pretty slow,
2
+
2+
2
2
+
Ba clearly improved the catalytic efficiency of Pd(OAc)
adding Zn(OTf) to Pd(OAc) improved the yield of indole up to 71.0%
with 74.2% conversion. However, in the case of trivalent metal ions
2
; in particular,
2 2
however, adding Zn(OTf) to Pd(OAc) greatly accelerates the dehydro-
genation reaction and demonstrates a higher yield of the 2-
methylindole product.
The catalytic dehydrogenation of other N-heterocyclic compounds
which contain secondary amine functional groups also clearly supports
2
2
like Sc3 and Al , the catalytic efficiency slightly decreased, giving
+
3+
6
1.9% and 55.4% of indoline conversion with 49.0% and 44.2% yield of in-
dole, respectively. This phenomenon is different from those observed in
Wacker-type oxidation, olefin isomerization and indole coupling reac-
tions in which a stronger Lewis acid can offer better promotion effect
that adding Zn(OTf)
by Pd(OAc) catalyst. For examples, in dehydrogenation of 1,2,3,4-
tetrahydroquinoline, adding Zn(OTf) offered 59.8% conversion with
55.1% yield of quinoline in 12 h at 353 K, whereas using Pd(OAc) alone
as catalyst only provided 36.2% of conversion with 23.6% yield of quino-
line (Table 2). The relatively low conversion of substrate can be attributed
2
greatly accelerates the dehydrogenation reaction
2
2
3
+
[
15,17,18]. Here, the lower efficiency of strong Lewis acid like Sc
2
3
+
and Al
can be attributed to its interaction with indoline substrate
and indole product which is basic. As shown in entry 9 in Table 1, adding
−
6
equiv. of NaOTf, which contains identical amounts of OTf anion as
those in 2 equiv. of Sc(OTf) , does not improve the catalytic efficiency
of Pd(OAc) , whereas 2 equiv. of Zn(OTf) significantly improved the
to the plausible interaction of indole product with Pd(OAc)
which blocks the promotion effect by added Lewis acid. In the case of 2-
methylindoline, adding Zn(OTf) to Pd(OAc) provided 74.0% yield of 2-
methylindole with 97.6% conversion of substrate, while Pd(OAc) alone
2
catalyst
3
2
2
2
2
−
dehydrogenation efficiency. To exclude the role of OTf anion in cataly-
2
sis, we further conducted complimentary experiments for Zn2 with
+
gave 43.2% yield with 51.0% conversion. In particular, in a 1 g scale dehy-
drogenation of 2-methylindoline, a 79.7% yield of 2-methylindole was
achieved. In a complementary test, tetrahydrothiopene was employed
as substrate, and it provided only 5% of thiopene as product. However,
in the absence of Lewis acid, no formation of thiopene was observed,
other counter-ions. While Zn(OAc)
soluble in acetonitrile, Zn(NO is soluble, and it demonstrated similar
promotional effect as well as Zn(OTf) , providing 62.8% yield of indole
with 95.2% of conversion. It clearly demonstrated that it is non-redox
2 4 3 2
, ZnSO , ZnCO and Zn(OH) are in-
3 2
)
2
2
+
−
metal ion like Zn , rather than OTf , plays the significant role in accel-
thus also evidenced the promotional effect of Lewis acid in Pd(OAc)
2
cat-
erating Pd(II)-catalyzed dehydrogenation. In addition, minor palladium
alyzed oxidative dehydrogenation.
black was observed after reaction in the case of using Pd(OAc)
lyst or adding NaOTf to Pd(OAc) , while adding other bivalent or triva-
lent Lewis acid to Pd(OAc) prevented the palladium black formation,
which is similar to those observed in Lewis acid promoted Wacker-
type oxidation by Pd(OAc) catalyst [15]. It is worth to mention that
2
as cata-
As reported elsewhere, a stronger Lewis acid may have a better pro-
2
motional effect on the redox metal ion mediated oxidations [10–14].
Here, due that the strong Lewis acid like Sc3 and Al
+
3+
can interact
2
with the tested N-heterocyclic compounds and related products which
are basic, the promotional effect of trivalent Lewis acids was not
2
added Lewis acid alone does not catalyze dehydrogenation as shown
in the parentheses of Table 1. In certain cases, the trace metal impurities
played significant roles in catalysis [19–22]. In our studies, the control
Pd(OAc) +Zn(OTf)
2 2
Pd(OAc)2
Zn(OTf)2
w
i
t
h
o
u
t
P
d
(
O
A
c
)
a
n
d
Z
n
(
O
T
f
)
Table 1
100
2
2
Lewis acid promoted oxidative dehydrogenation of indoline to indole.
8
0
0
6
Entry
Catalyst
Lewis acid
Conv. %
Yield %
1
2
3
4
5
6
7
8
9
–
–
–
13.2
38.7
10.8
34.3
40
20
0
Pd(OAc)
Pd(OAc)
Pd(OAc)
Pd(OAc)
Pd(OAc)
Pd(OAc)
Pd(OAc)
Pd(OAc)
2
2
2
2
2
2
2
Sc(OTf)
Al(OTf)
Zn(OTf)
Ca(OTf)
Mg(OTf)
Ba(OTf)
6NaOTf
3
61.9(12.4)
55.4(17.0)
74.2(13.8)
65.8(15.3)
52.5(12.9)
70.5(14.1)
38.8(11.3)
49.0(9.2)
44.2(12.9)
71.0(11.2)
62.4(13.2)
37.8(7.8)
67.4(8.4)
34.7(6.0)
3
2
2
2
0
50
100
150
200
2
2
Time / min
Conditions: Pd(OAc)
loon, 353 K, 6 h. The data in parentheses represent the control experiment without
Pd(OAc)
2 3 2
1 mM, Lewis acid 2 mM, CH CN 5 mL, Substrate: 100 mM, O bal-
Fig. 1. Time course of dehydrogenation from 2-methylindoline. Conditions: Pd(OAc)
1 mM, Lewis acid 2 mM, CH CN 5 mL, substrate 100 mM, O balloon, 353 K.
2
2
.
3
2