Chemistry Letters Vol.33, No.7 (2004)
809
action time (Entry 5) can remarkably enhance the conversion of
benzene. It is very interesting, however, to observe a slight de-
creasing of the conversion of benzene when the amount of ionic
liquid is raised (Entries 1, 6, and 7).
tric acid could be easily kept at a suitable level when high con-
centrated or fuming nitric acid is employed to replenish the con-
sumed nitric acid.
The nature of the Brꢀnsted ionic liquids catalyzed nitration
of aromatic compounds is not clear at this stage. The classical
reaction mechanism of nitration of benzene in the presence of
Then ionic liquid 1 is employed as catalyst for nitration of
some other aromatic compounds, including toluene, chloroben-
zene, and bromobenzene with 62% nitric acid under unopti-
mized reaction conditions (Entries 8–10), in all of these cases,
medium to high conversions of aromatic compounds are also
achieved. When nitrobenzene is used as substrate, no reaction
is observed, which is in accord with the above results (Entry 11).
Once the reaction is over, our attention is paid to the issues
of product separation and recycling of the Brꢀnsted ionic liquids.
This nitrating system is carried out in a biphasic mode, so it is
very easy to perform the product separation by decantation or us-
ing an extraction funnel after reaction.
From the point of manufacturing view, a continuous reaction
process without catalyst separation is very attractive in industry
in the case of nitration of aromatic compounds with nitric acid.
Then we examine the reusability of the remaining aqueous
phase, consisted of nitric acid and ionic liquid, in a way that di-
rectly employed it as catalyst for next run, just replenishing a
certain amount of 62% nitric acid to the aqueous phase. Results
of recycling of nitration of benzene with nitric acid, under the
same reaction condition as Entry 2 of table 1, are listed in
Table 2. During the whole process, the mole ratio of benzene
to nitric acid is kept at 1:2. It should be noted out, however,
the concentration of nitric acid decreased steadily with the reac-
tion goes on owing to the accumulating of water, which is
formed as waste product and not separated from the system.
As can be seen from the table, with the decreasing of the concen-
tration of nitric acid, conversion of benzene decreased simulta-
neously, but it can still kept at 25.6% after 5 times recycle and
the concentration of nitric acid decreased even to about 36%,
which suggesting the Brꢀnsted ionic liquid might has a great
possibility to be applied in large scale as the concentration of ni-
1
mixture acid of nitric acid and sulfuric acid is well established,
þ
which involved the formation of NO2 as nitrifier at first and
þ
then followed by electrophilic addition of NO2 with benzene.
Because the Brꢀnsted ionic liquids have the sulfuric acid-like
group –SO3H in their molecular structure, we are inclined to be-
lieve that the traditional reaction mechanism also functions here.
In conclusion, it is demonstrated that the Brꢀnsted ionic liq-
uids are a kind of novel and reusable catalysts for nitration of
simple aromatic compounds with aqueous nitric acid. The reac-
tion is carried out under solvent-free condition in a biphasic
mode. In comparison with other nitrating system, it is a more
green process with promising prospect for practical application.
References
1
For books and reviews on nitration, see a) J. G. Hoggett,
R. B. Moodie, J. R. Penton, and K. Schofield, ‘‘Nitration
and Aromatic Reactivity,’’ Cambridge University Press,
London (1971). b) G. A. Olah, R. Malhotra, and S. C.
Narang, ‘‘Nitration: Methods and Mechanisms,’’ VCH
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Paukshtis, and K. G. Ione, Catal. Rev.—Sci. Eng., 1995, 179.
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ences cited therein.
2
3
4
F. J. Waller, A. G. M. Barrett, D. C. Braddock, and D.
Ramprasad, Chem. Commun., 1997, 613.
For recent reviews on ionic liquids, see a) J. Dupont, R. F. de
Souza, and P. A. Z. Suarez, Chem. Rev., 102, 3667 (2002). b)
P. Wasserscheid and W. Keim, Angew. Chem., Int. Ed., 39,
a
Table 2. Recycling of ionic liquid 2 for nitration of benzene
3
772 (2000). c) T. Welton, Chem. Rev., 99, 2071 (1999).
Benzene/
nitric acid
Concentration of
nitric acid/%
Conversion
/%
Run
d) C. M. Gordon, Appl. Catal., A, 222, 101 (2001). e) R.
A. Sheldon, Chem. Commun., 2001, 2399.
a) K. K. Laali and V. J. Gettwert, J. Org. Chem., 66, 35
1
2
3
4
5
1:2
1:2
1:2
1:2
1:2
62
51
45
40
36
76.5
65.2
52.1
37.5
25.6
5
6
(
8
2001). b) S. T. Handy and C. R. Egrie, ACS Symp. Ser.,
18, 134 (2002).
A. C. Cole, J. L. Jensen, I. Ntai, K. L. T. Tran, K. J. Weaver,
D. C. Forbes, and J. H. Davis, Jr., J. Am. Chem. Soc., 124,
5962 (2002).
a
The reaction condition is same as Entry 2 of Table 1.
Published on the web (Advance View) June 7, 2004; DOI 10.1246/cl.2004.808