S. Rostamnia et al. / Tetrahedron Letters 53 (2012) 5257–5260
5259
γ-Fe2O3@SiO2-OSO3H
N
S
S
N
(1 mol%)
O
NH2
N
C
solvent-free
35 oC, 1 h
N
3
6
2
5
87%
NHCyHex
Scheme 2. The use of
c
-Fe2O3@SiO2-OSO3H for the synthesis of aminoimidazothiazole 6.
To demonstrate the diversity of the
c
-Fe2O3@SiO2-OSO3H nano-
catalyst and to expand the scope of the process, the optimized con-
ditions were applied to a series of substrates 1, 2, and 3 as shown in
Table 4.
OSO3H
N
2
4
Ar
N
Solid Acid
The catalytic activity of
c-Fe2O3@SiO2-OSO3H in the Ugi-like
NR
Groebke-Blackburn-Bienaymé three-component synthesis of an
aminoimidazothiazole was also studied under the optimized con-
ditions. The yield of the designed product 6 was 87% after 1 h
(Scheme 2).
Although we have not established the exact mechanism for this
reaction in the presence of c-Fe2O3@SiO2-OSO3H in an experimental
manner, a possible explanation for the synthesis of 3-aminoimi-
dazo[1,2-a]pyridines 4, based on an isocyanide-based multicompo-
nent reaction12–20,30–32 is proposed in Scheme 3.
SiO2
γ-Fe2O3
H
O3SO
=
N
N
OSO3
H
O
C
Ar
N
1
Ar
R
3
In summary, covalent functionalization of sulfuric acid onto
H2O
O3SO
H
N
N
magnetic
c-Fe2O3@SiO2 nanoparticles has successfully been
achieved. An extensive and systematic study identified
c
-Fe2O3@-
Ar
SiO2-OSO3H as a heterogeneous, green, and reusable catalyst for
the synthesis of aminoimidazopyridines via an Ugi-like (isocya-
nide-based) three-component reaction. A variety of annulated ami-
noimidazoles are accessible under mild conditions using this
method. This rapid, green method in which the catalyst can be
recycled might serve as an interesting alternative to other
synthetic methods. The aminoimidazole products are of potential
synthetic and pharmaceutical interest.
Scheme 3. A plausible mechanism for the Ugi-like MCR using
c-Fe2O3@SiO2-
OSO3H.
pyridine, and an isocyanide using SO3H-functionalized magnetic
iron oxide as the catalyst.
The maghemite nanoparticles (c-Fe2O3, Fig. 1) were synthesized
by a chemical co-precipitation technique using ferric and ferrous
ions.21–23 Based on our previous reports,6,21–23 coating a layer of
Acknowledgment
silica on the surface of the c-Fe2O3 nanoparticles and then func-
We gratefully acknowledge funding support from the Univer-
sity of Maragheh.
tionalization of the iron oxide with a sulfonic acid group were
achieved by treatment with tetraethyl orthosilicate [(EtO)4Si,
TEOS] followed by chlorosulfonic acid (0.60 mmol gꢀ1 –SO3H load-
ing, see Supplementary data).
Supplementary data
In order to investigate the catalytic activity and application of
c
-Fe2O3@SiO2-OSO3H in the Ugi-like multicomponent synthesis
Supplementary data associated with this article can be found, in
of imidazopyridines,4,29 we examined its efficiency in a model
reaction between 2-aminopyridine, benzaldehyde, and cyclohexyl
isocyanide. Due to the fact that the solvent may play an important
role in this process, various solvents were screened. The model
reaction was examined in methanol, ethanol, and water using 2%
References and notes
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mol of c-Fe2O3@SiO2-OSO3H (Table 1). However, when the reaction
was run under solvent-free conditions, the product was obtained in
92% yield at 35 °C in 1 h; the yield increased sharply when the tem-
perature was raised from room temperature to 35 °C.
Next, the model reaction of 2-aminopyridine with benzalde-
hyde and cyclohexyl isocyanide under solvent-free conditions
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was carried out using different amounts of
c-Fe2O3@SiO2-OSO3H
as the catalyst (Table 2). A very high yield of 3-aminoimi-
dazo[1,2-a]pyridine (92%) was obtained with 1 mol % of the cata-
lyst. A further increase in the amount of catalyst (up to 5 mol %)
and of the reaction temperature did not have any significant effects
on the product yield or reaction time.
12. Groebke, K.; Weber, L.; Mehlin, F. Synlett 1998, 661.
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3635.
The possibility of recycling the magnetic catalyst was also stud-
ied. When the reaction was complete, the catalyst was easily sep-
arated from the product by applying a magnet to the exterior of the
reaction vessel. As illustrated in Table 3, the catalyst could be re-
used without any significant loss in the yield over five runs. After
the fifth run the turnover number (TON) was 453.