94
S.M. Sadeghzadeh / Catalysis Communications 72 (2015) 91–96
Fig. 4. (a) Effect of the amount of the catalyst on yield of quinazoline-2,4(1 H,3 H)-dione; (b) Effect of temperature on yield of quinazoline-2,4(1 H,3 H)-dione; (c) Effect of CO
2
pressure
dependence with KCC-1/IL NPs catalyst system; and (d) Effect of time on yield of quinazoline-2,4(1 H,3 H)-dione.
supported catalyst gave the desired product in excellent yield (97%) due
to the formation of by-products (Table 3, entry 5). Comparison of KCC-
We compared the catalytic performance of our catalyst with litera-
ture reported catalysts for the synthesis of quinazoline-2,4(1 H,3 H)-
dione (Table 6). Table 6 clearly demonstrates that lower temperature,
the minimum amount of catalyst, lower pressure of carbon dioxide
and shorter reaction time were required for the synthesis of
quinazoline-2,4(1 H,3 H)-dione, using KCC-1/IL NPs, while an appropri-
ate, highly perfect, performance of the present catalyst was observed for
this reaction.
1
4 4
/IL/BF with other ionic liquid, demonstrates the advantage of BF as
anion obtained the highest efficiency.
Having proved correct and complete synthesis of the catalysts, the
catalysts performance and stability with the synthesis of quinazoline-
2
,4(1 H,3 H)-dione tested. In order to optimize the reaction conditions
and obtain the best catalytic activity, the reaction of CO and 2-
2
aminobenzonitrile was used as a model, and was conducted under dif-
ferent reaction parameters such as amount of the catalyst, temperature,
time, and solvent. Initially, the model reaction was carried out in several
solvents to investigate the efficiency of the catalyst. In this study, it was
found that conventional heating at 70 °C under solvent-free (Table 4) in
These observations indicated that the catalysts were stable and
could tolerate the present reaction conditions. The recyclability of cata-
lysts was examined using the model reaction under identical conditions.
After the required time, the catalysts were recovered from the reaction
mixture by filtration, washed with ethyl acetate, and subsequently dried
at 100 °C then reused. After ten consecutive reuses, KCC-1/IL NPs exhib-
ited almost identical catalytic activity (Fig. 5a). The recyclability test was
stopped after ten runs. Comparison of TEM images and FT-IR spectra
(Figs. 1c and 5b) of used catalyst with those of the fresh catalyst (Figs.
1a,b and 2b) showed that the morphology and structure of KCC-1/IL
NPs remained intact after ten recoveries. In order to know whether
the reaction takes place at the surface of KCC-1/IL NPs or any IL species,
ICP analysis of the remaining mixture after catalyst and product separa-
tion was investigated upon reaction completion. The amount of ionic
liquid leaching after the ten repeated recycling was 4.2%. These
6
2
0 min at 0.8 bar CO pressure in the presence 0.0007 g of KCC-1/IL is
more efficient, with respect to reaction time and yield of the desired
quinazoline-2,4(1 H,3 H)-dione (Fig. 4).
Since KCC-1/IL NPs were the most active of the one-component cat-
alysts, they were tested in the conversion of six other terminal 2-
aminobenzonitriles (1a–f) into the synthesis of quinazoline-
2
5
,4(1 H,3 H)-diones (2a–f) (Scheme 1), results being shown in Table
. In each case, the quinazoline-2,4(1 H,3 H)-diones were obtained
with good to excellent isolated yield after 1 h using 0.0007 g of catalyst
under solvent-free conditions at 70 °C under a constant pressure of car-
bon dioxide.
Table 5
a
Synthesis of quinazoline-2,4(1 H,3 H)-dione derivatives catalyzed by KCC-1/IL NPs.
Entry
R
Product
Yield (%)b
1
2
3
4
5
6
H
Br
F
Cl
Me
NO
2a
2b
2c
2d
2e
2f
97
91
94
92
88
96
2
a
Reaction condition: 2-aminobenzonitrile derivatives (1 mmol), KCC-1/IL NPs (0.0007 g),
Scheme 1. Synthesis of quinazoline-2,4(1 H,3 H)-diones from CO
aminobenzonitriles.
2
and 2-
CO
2
0.8 MPa, 1 h.
Yield refers to isolated product.
b