Synthesis of pyranopyrazoles
1015
1
54.74, 155.72, 160.68; Anal. Calcd for C H N O : Table 2. Eaffects of different solvents on the reaction
15
14
4
2
C, 63.82; H, 5.00; N, 19.85. Found: C, 63.24; H, 4.87; productivity .
N, 19.81.
Entry
Catalystb
Solvent
Time Yield (%)
1
2
3
4
Acidic ionic liquid
Acidic ionic liquid
Acidic ionic liquid
–
0.5 h
1 h
1 h
75
67
55
–
2
.3b 6-Amino-4-(4-methylphenyl)-3-methyl-2,4-
Water
Ethanol
dihydropyrano[2,3-c]pyrazole-5-carbonitrile (2j):
◦
−1
Mp 175–177 C. FTIR (KBr,cm ): υ = 3448.78 (NH),
Acidic ionic liquid Acetonitrile 24 h
3418.4 and 3353.51 (NH ), 2188.78 (CN), 1624.91
2
a4-Chlorobenzaldehyde/ethylacetoacetat/hydrazine hydrate/
1
(
C=N), 1579.37 (C=C); H NMR (400 MHz, DMSO-
malonitrile (1:1:1:1 mmol)
d ): δ = 1.8 (s, 3H, CH3), 2.28 (s, 3H, Ar-CH3), 4.52
b
6
0
.15 mmol
(s, 1H, C-4 pyran), 6.85 (d, 2H, p-tolyl-H), 7.00 (d, 2H,
p-tolyl-H), 7.18 (s, 2H, NH2), 12.09 (s, 1H, NH);
13
Table 3. Optimization of amount of catalyst for synthesis
of pyranopyrazol from 4-chlorobenzaldehyde .
C NMR (75 MHz, DMSO-d ): δ = 9.9, 20.7, 36.7,
6
a
4
0.1, 78.3, 97.4, 120.7, 127.2, 128.6, 135.4, 140.9,
1
54.7, 160.6; Anal. Calcd for C H N O: C, 67.65;
15
14
4
Catalyst
(mmol)
Time
(min)
H, 5.30; N, 21.04. Found: C, 67.15; H, 5.17; N, 21.00.
Entry
Yield
1
2
3
4
5
6
0.05
0.10
0.15
0.20
0.25
0.30
30
30
30
30
30
30
50
65
75
81
85
85
3
. Results and discussion
Several methods are used in the synthesis of these
dihydropyrano[2,3-c]pyrazole derivatives. In addition,
the synthesis of these heterocycles has been usually
carried out in polar organic solvents such as water, a4-Chlorobenzaldehyde/ethylacetoacetat/hydrazine hydrate/
malonitrile (1:1:1:1 mmol)
ethanol, DMF and DMSO leading to complex isolation
and recovery procedures. These processes also gene-
rate waste containing catalyst and solvent, which have
Table 4. Synthesis of substituted pyranopyrazoles using
to be recovered, treated and disposed of.7 The toxi-
,28
[(CH2)4SO3HMIM][HSO4] (0.25 mmol) as a catalyst under
city and volatile nature of many organic solvents, par- solvent-free conditions.
ticularly chlorinated hydrocarbons that are widely used
◦
Mp/ C
Found Reported
in huge amounts for organic reactions have posed a
serious threat to the environment.29 Thus, design of Producta
solvent-free catalytic reaction has received tremendous
R
Yields (%)b
30
2a
4-ClPh
3-ClPh
2-ClPh
4-MeOPh
Ph
4-BrPh
3-BrPh
4-NO2Ph
3-NO2Ph
4-MePh
85
80
80
85
80
80
80
90
85
90
173–175 174–1757
157–158 158–1607
attention in recent times in the area of green synthesis.
2
2
2
2
b
c
d
e
The choice of a solvent is a crucial factor for mul-
ticomponent reactions. So at the first step we looked
into the solvent effect for this reaction. We tested
7
145–147 145–146
171–173 170–1727
7
166–168 167–169
181–183 180–1837
the reaction in some protic and aprotic solvents such 2f
2
2
2
2
g
h
i
177–179
–
as ethanol, water and acetonitrile in the presence of
(CH ) SO HMIM][HSO ] as a catalyst. The reaction
193–194 192–1947
190–193 190–1927
175–177 175–1767
[
2
4
3
4
in the aprotic solvent had satisfying performance but
in the aprotic solvent (acetonitrile) efficiency was poor,
even after 24 h. Also the reaction was carried out at
the solvent-free conditions. By omitting the solvent, the
productivity of the reaction was better and addition-
ally, the reaction time decreased. The related results are
given in table 2. Hence, in the next steps we have used
j
a
All the isolated products were characterized on the basis of
their physical properties and IR, H- and C-NMR spectral
analysis and by direct comparison with authentic materials
1
13
b
Isolated yields
the solvent free conditions for synthesis of substituted of 4-chloro benzaldehyde (1 mmol), ethyl acetoacetate
pyranopyrazoles. (1 mmol), hydrazine hydrate (1 mmol), malononitrile
Apart from the solvent, the efficiency of the multi- (1 mmol) and [(CH ) SO HMIM][HSO ] (0.05 mmol),
2
4
3
4
component reactions is mainly affected by the amount as a catalyst at room temperature for 30 min, which
of catalyst and the reaction time. In the next stage for led to low yield (55%) of the product. To enhance the
getting the best conditions, we started the condensation yield of the desired product, the amount of catalyst was