2
(not final pg. №)
J. R. LI and Y. L. HU: Benzotriazolium Ionic Liquid Immobilized …
4 10 2 3
was only bulk ionic liquid of ILC H O NiCl or ILCl and PMO
support catalysts (Table 1, entries 6–8). Therefore,
PMO@ILC NiCl (1.0) is thought to the suitable cata-
4
H
10
O
2
3
lyst for the reaction. Then, the effect of catalyst dosage on
the cycloaddition was examined. The yield of propylene
carbonate increased with the catalyst amount of the cata-
lyst was increased from 5 mg to 20 mg (Table 1, entries 4,
1
0-12), while a further increase in the catalyst amount did
not gave more product (Table 1, entries 13 and 14). There-
fore, the best result was obtained with 20 mg catalyst.
The effect of the reaction temperature on the
Scheme ꢀ. Catalytic synthesis cyclic carbonates from CO
and epoxides with PMO@ILC NiCl
2
4
H
10
O
2
3
.
cycloaddition
PMO@ILC
was
NiCl
studied
over
the
catalyst
4
H
10
O
2
3
(1.0), and the results are revealed in
easy recovery and recyclable ionic liquid-based heteroge-
neous catalysts are always in demand. Immobilization of
Ionic liquids onto porous solid supports to explore hetero-
geneous supported ILs has gained comprehensive atten-
Figure 1. As shown in the figure, the yield and selectivity of
propylene carbonate were significantly increased with the
increase of reaction temperature. While, the temperature
was further increased from 110°C to 130°C, the yield and
selectivity of propylene carbonate showed a slight
decrease. The reason may be that the overly high
of isomerization and ring opening of propylene oxide,
which was determined by GC analysis. These results
indicated that the suitable temperature was 110 °C. The
Among these soild supports, periodic
mesoporous organosilicas (PMOs) have attracted increas-
ing attention because of their combined advantages of
large specific surface areas, tunable pore sizes, uniform
distribution of functional groups, chemical and thermal sta-
bilities, as well as highly ordered mesostructure proper-
As part of our ongoing interest in the
development of efficient and environmentally friendly cat-
alytic systems, herein, we intend to perform immobilization
of benzotriazolium ionic liquid onto periodic mesoporous
organosilica to design multifunctional immobilized ionic liq-
2
Table 1. Catalyst screening for CO cycloaddition to
propylene oxide.
(
a)
Catalyst / Time / Yield / Selectivity /
Entry
Catalyst
PMO@ILC
(
b)
(b)
uids. The obtained PMO@ILC
ionic liquid concentration have been employed as hetero-
geneous and recyclable catalysts in the cycloaddition of CO
4
H
10
O
2
NiCl
3
with different
mg
h
%
%
4 10
H
1
2
3
4
5
20
5
5ꢇ.ꢅ
8ꢂ.ꢆ
9ꢄ.ꢈ
9ꢈ.ꢀ
9ꢈ.ꢄ
99.ꢅ
99.ꢆ
99.ꢄ
99.7
99.4
O
2
NiCl (ꢅ.ꢆ)
PMO@ILC
NiCl (ꢅ.6)
PMO@ILC
NiCl (ꢅ.ꢁ)
PMO@ILC
NiCl (ꢀ.ꢅ)
PMO@ILC
NiCl (ꢀ.ꢂ)
NiCl
3
2
4 10
H
20
20
20
5
with epoxides under cocatalyst- and solvent-free condi-
tions (Scheme 1). Additionally, the recyclability and reusa-
bility of the catalyst was also investigated.
O
2
3
H
4 10
3.ꢈ
3.ꢈ
3.ꢈ
O
2
3
H
4 10
O
2
3
RESULTS AND DISCUSSION
H
4 10
20
O
2
3
The catalytic activities of PMO@ILC
tested in the model reaction of CO
propylene oxide to produce propylene carbonate. As shown
in Table 1, the efficiency of PMO@ILC NiCl with
different ionic liquid concentration was screened. The
immobilized ILs catalysts include PMO@ILC NiCl (0.4),
PMO@ILC NiCl (0.6), PMO@ILC NiCl (0.8),
PMO@ILC NiCl (1.0), and PMO@ILC NiCl (1.2)
4 10
H O
2
NiCl
3
(x) were
20(c)
6
7
8
9
ILC
4
H
10
O
2
3
12
12
12
24
89.ꢈ
46.7
24
9ꢆ.ꢈ
9ꢀ.ꢄ
93.1
0
2
cycloaddition with
ILCl
20(c)
20(c)
–
PMO
H O
4 10 2
3
–
0
H O
4 10 2
3
PMO@ILC
NiCl
PMO@ILC
NiCl (ꢀ.ꢅ)
PMO@ILC
NiCl (ꢀ.ꢅ)
PMO@ILC
NiCl (ꢀ.ꢅ)
PMO@ILC
NiCl (ꢀ.ꢅ)
4
H
(ꢀ.ꢅ)
4 10
H
10
1
0
5
6
4ꢄ.ꢇ
8ꢄ.ꢂ
9ꢂ.ꢀ
9ꢈ.ꢅ
9ꢆ.ꢇ
99.4
99.3
99.4
99.3
99.1
O
2
3
4
H
10
O
2
3
4
H
10
O
2
3
4
H
10
O
2
3
4
H
10
O
2
3
11
10
15
25
30
4
O
2
3
could significantly enhance the catalytic activity of cycload-
dition (Table 1, entries 1–5), and PMO@ILC NiCl (1.0)
showed the highest catalytic activity with 95.1 % yield and
9.7 % selectivity (Table 1, entry 4). It was found that the
H
4 10
1
2
3
3.ꢈ
3.ꢈ
3.ꢈ
4
H
10
O
2
3
O
2
3
H
4 10
1
O
2
3
9
H
4 10
reaction did not accomplished in the absence of catalyst,
even the reaction time was prolonged to 24 h (Table 1, en-
try 9). For comparison, it was also observed that the
cycloaddition could not be carried out successfully if there
14
O
2
3
(a) Reaction conditions: propylene oxide (10 mmol), CO (ꢀ.ꢅ MPa), catalyst,
2
1
10 °C.
Determined by using GC;
(c) Reaction temperature is 150 °C.
(b)
Croat. Chem. Acta 2020, 93(2)
DOI: 10.5562/cca3668