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YUTILOV et al.
ly insoluble in water. After the bromination comple-
tion, the acetic acid was distilled off almost to dry-
ness, and water was added to the residue. By-product
VI remained in the insoluble residue, and it was fil-
tered off. By alkalization of the filtrate, we isolated
virtually pure III, without impurity of VI.
obtain pure nitro compound IV after the transforma-
tion of X in concentrated sulfuric acid, the acid solu-
tion after the nitration was neutralized with sodium
acetate. After adding a half of the amount of sodium
acetate required for complete neutralization of the
reaction mixture, a bright yellow precipirtate of IV
containing no by-products is formed. Neutralization of
the filtrate after the isolation of IV to pH 6 7 allows
isolation of the precipitate of dibromo derivative VI.
If salt X taken for the nitration is free of amine VI,
almost quantitative yield of IV can be attained, and its
purity considerably increases. After recrystallization of
IV from DMF, its melting point increases by 2 3 C
The nitration of amine III under the conditions de-
scribed in [1, 2] often yielded, instead of the expected
nitro compound IV, a black precipitate from which we
failed to isolate the desired product by recrystalliza-
tion from solvents in the presence of activated carbon
or alumina, or by reprecipitation with alkalis from
weakly acidic solutions. In nitration of 2-amino-5-
bromopyridine VII under the same conditions, a sig-
nificant amount of 3-nitro-5-bromo-2-pyridone VIII
is formed along with the desired 3-nitro derivative of
VII [13].
(mp 213 C).
When in nitration of III HNO is replaced by a less
3
aggressive and more convenient in handling agent,
e.g., KNO in concentrated H SO , the reaction at
3
2
4
0
4
10 C yields no nitro compound IV, and heating to
0 50 C causes formation of pyridone IX. The nitra-
Nitration of III under the similar conditions is also
accompanied by deamination. From dark tarry prod-
ucts, we isolated a compound identified as 3-nitro-5-
bromo-6-methyl-2-pyridone IX.
tion of III in glacial acetic acid also gives negative
results.
According to [1, 2], nitro compound IV is reduced
to diamine V with hydrogen in the presence of Raney
nickel. Despite a fairly high yield of V, 70%, this
procedure is not quite feasible for industrial applica-
tion, because the catalyst is pyrophoric and hydrogen
is dangerously explosive. In the reduction of IV with
To avoid formation of IX in nitration of III, we
changed the order of mixing the reactants. Fuming
nitric acid was added to a solution of III in sulfuric
acid not at 55 60 but at 0 5 C, after which the
temperature was gradually raised to 55 60 C. By
so doing, we considerably reduced the yield of tars.
However, after recrystallization of the products from
methyl ethyl ketone, we detected IX in an amount
comparable with that of the target product. By-product
IX is insoluble in methyl ethyl ketone, alcohol, water,
and the majority of aprotic solvents. At decreased
nitration temperatures, the amount of IX decreased
considerably (to 5 10 wt % relative to IV).
SnCl in concentrated HCl according to [12], the yield
2
of V does not exceed 60%, and diamine V is contam-
inated with by-products and requires additional purifi-
cation. Taking into account the fact that structurally
related 2-amino-3-nitro-5-chloro(bromo)-6-methylpy-
ridine is smoothly reduced with sodium sulfide in
aqueous solution [10], we examined the applicability
of this procedure to the reduction of IV at 60 100 C.
At 60 C, no reduction occurs, and at 100 C the reac-
tion is accompanied by extensive tarring. At 75 80 C,
the yield of V does not exceed 40%. Experiments on
reduction of IV with iron in aqueous solution contain-
ing a small amount of HCl showed that, when iron
dust is added in small portions to a solution of IV at
We examined the influence exerted by the condi-
tions of nitration of III on the composition of the
reaction products. It is advisable to perform nitration
at 0 5 C in concentrated sulfuric acid with 60 63%
nitric acid. In isolation of the desired nitro compound
IV, to avoid formation of tarry impurities, the mixture
should be neutralized to pH 2 3 with sodium acetate;
in this case, the yield of IV is 80 85%. However,
even with all these conditions observed, a certain
amount of tar is formed; it decreases the melting point
of IV by 10 20 C. Even a slight excess of nitric acid
in nitration of amine III causes strong darkening of
IV. For accurate dosage of nitric acid in nitration, we
used instead of amine IV its nitrate X and added this
salt with vigorous stirring at 15 C to concentrated
sulfuric acid. Salt X is readily formed by mixing a
melt of III with 60 63% nitric acid in water. Salt X
can be obtained from crude III without its drying. To
80 90 C, the reduction occurred readily without self-
heating and could be controlled. The yield of V
reached 80% and did not decrease when the reaction
time and amount of iron were decreased by half.
The most efficient is the reduction of IV with
hydrazine hydrate. Refluxing of IV with a 15-fold
excess of hydrazine hydrate for 5 6 h results in the
formation of V in 68 70% yield. When the process is
performed in a solvent, the consumption of hydrazine
hydrate can be decreased by a factor of more than 3.
1-Butanol appeared to be the best solvent for this
RUSSIAN JOURNAL OF APPLIED CHEMISTRY Vol. 78 No. 5 2005