Bjørsvik et al.
SCHEME 6
for the compound carrying an acetyl group (28), it was
only the 2,2′-dinitrobiphenyl substituted with the -COOH
group (compound 26) that provided a low yield. The
corresponding methylester (27) of that compound and
2,2′-dinitrobiphenyl derivative 29 both provided accept-
able yields (∼50%). All of the other 2,2′-dinitrobiphenyl
derivatives provided excellent yields.
is <140 °C, the redox process did not operate; see, e.g.,
experiment entry 14. (ii) When elevated temperatures are
utilized, high conversions of 2,2′-dinitrobiphenyl 6 are
accomplished, but most probably this is due to successive
degradation reactions. Moreover, when the process is
carried out at reaction temperatures that exceed 170 °C,
the solvent cage that encloses the reactive species may
be weakened, which results in leakage of the reactive
species that can provide other reduction products or tars.
We believe that the disclosed process can find applica-
tion for synthetic purposes, even if the process requires
a slightly elevated temperature to operate satisfactory.
The elevated temperature is a minor drawback compared
to the advantages of the novel process: (i) the process
operates in the absence of any transition (or heavy)
metals in catalytic or stoichiometric quantities, (ii) no
toxic or hazardous reagents are required, (iii) the process
is operated with cheap reagents and solvents, (iv) the
novel process provides as high selectivity and yield as
the most of the other processes and methods previously
disclosed by other researchers,18-24 and (v) no harmful
side products are produced during the process. In all, the
disclosed process appears to be an attractive method for
benzo[c]cinnolins and may thus provide an alternative
for industrial applications.
Con clu sion s
A process leading to benzo[c]cinnoline 10 and benzo-
[c]cinnoline N-oxide 11 has been discovered and inves-
tigated. During the investigation of the process it was
discovered that the types of solvent and base were of
paramount importance for the course of the process.
Likewise, the reaction temperature should carefully be
kept within the range 155-167 °C to achieve optimal
yields. The quantity of acetophenone, which functions as
a reductant, should, when using the process for the
preparation of benzo[c]cinnoline 10, be used in slightly
less than molar quantities. When synthesizing benzo[c]-
cinnoline N-oxide 11 a moderate molar excess of ac-
etophenone is required. When the optimized experimen-
tal conditions are used, excellent selectivity and yields
are achieved for either of the two products, namely 93%
(10) and 91% (11). The novel process to benzo[c]cinnoline
can successfully be utilized for the preparation of various
substituted benzo[c]cinnolines in most cases with me-
dium to high yields, Table 2. As for the previously
disclosed catalytic aerobic oxidation process,1,2 the novel
combined redox and cyclization process forming the
benzo[c]cinnoline framework is not compatible with
functional groups such as -CN, -NH2, and -OH, as such
groups easily forms free radicals under the redox condi-
tions and result in nonselective processes: these form
only degradation products or tars.
We believe that the reaction proceeds by a complex
reaction mechanism, some facets of which are outlined
in Scheme 3. Likewise, we think that the initial redox
process (path (b), Scheme 2) forming the radicals is
analogous to the mechanisms we have previously dis-
closed.1-3 Additionally, the work of Russell and co-
workers6-,8 described conclusive evidence for the single
electron-transfer reduction of nitroarenes in basic
media, and for the formation of C-centered radicals and
nitroarene radical anions by reactions of carbanions with
nitroarenes.
Exp er im en ta l Section
Ben zo[c]cin n olin e: Wor k u p w ith F la sh Ch r om a tog-
r a p h y. The reaction was carried out in a sealed tube reactor
of 50 mL capacity. The reaction tube was flushed with
nitrogen, and the reactants 2,2′-dinitrobiphenyl (Aldrich 97%)
(2.0 mmol, 0.488 g) and acetophenone (1.8 mmol, 0.212 mL)
were dissolved in ethanol (15 mL) and placed in the reaction
tube. Finally, sodium ethoxide (10 mmol, 0.230 g) was added.
The reaction mixture was heated at 160 °C for 5 h and
quenched with water (50 mL) followed by filtration on Celite.
The filtrate was extracted with ethyl acetate (3 × 50 mL). The
organic phase, which contained the target product, was dried
over anhydrous sodium sulfate and filtered and the solvent
removed under vacuum to obtain the crude product (564 mg).
This material was purified and separated by means of stan-
dard flash chromatography25 using a column of i.d. 3 cm. The
eluent was ethyl acetate and n-hexane in the ratio 1:4 (Rf (10)
) 0.334, Rf(11) ) 0.182). The crude material (564 mg) was
(18) Ettienne, A.; Izoret, G. Bull. Soc. Chim. Fr. 1964, 2897.
(19) Everett, J . L.; Ross, W. C. J . Chem. Soc. 1949, 1972.
(20) King, F. E.; King, T. J . J . Chem. Soc. 1945, 824.
(21) Ross, S. D.; Kahn, G. J .; Leach, W. A. J . Am. Chem. Soc. 1952,
74, 4122.
(22) Laskar, D. D.; Prajapti, D.; Sandhu, J . S. J . Chem. Soc., Perkin
Trans. 1 2000, 67-69.
(23) Pink, M.; Young, V. G. J . Org. Chem. 2000, 65, 6388.
(24) Wada, S.; Urano, M.; Suzuki, H. J . Org. Chem. 2002, 67, 8254-
8257.
Experiments conducted at (i) prolonged reaction times
at low temperatures or (ii) at short reaction times with
elevated reaction temperature did not provide high yields
as anticipated by the response surface. Explanations for
this may be as follows: (i) When the reaction temperature
(25) Still, W. C.; Khan, M.; Mitra, A. J . Org. Chem. 1978, 43, 2923.
7726 J . Org. Chem., Vol. 69, No. 22, 2004