A NEW TECHNOLOGY FOR THE SYNTHESIS OF 4,5,6,7ꢀTETRAHYDROINDOLE
309
24.3 [12]). Therefore, for complete shift of equilibꢀ available on a multiꢀton scale using the nanocrystalꢀ
rium to complex IV, the resultant water was removed line aggregate composed of sodium cyclohexanone
as azeotrope with toluene. For convenience of catalyst oximate and its complex with DMSO as the catalyst.
dosage, it can be prepared as a solution in a mixture The high conversion (70–90%) of the starting comꢀ
with oxime III in DMSO, which remains homogeꢀ pounds (cyclohexanone oxime and acetylene) and
neous at 100–130°C (depending on the content of high selectivity (95–99%) toward the target product,
complex IV).
enhanced safety (the use of atmospheric or close to
atmospheric pressure of acetylene, the absence of
flammable and explosive diethyl ether extractant), and
improved environmental characteristics (lowꢀwaste
production) are the attributes of this technology.
Therefore 4,5,6,7ꢀtetrahydroindole becomes a real
starting material for its industrial dehydrogenation
into indole [14].
Moreover, the use of complex IV as catalyst instead
of free alkalis prevents the irreversible transformation
of the latter into acetates through the known reaction
[
13] with acetylene and water according to Scheme 5.
MOH + HC≡CH + H O
MOCOCH + H2
2
3
(
M is an alkali metal).
Scheme 5.
The general procedure of indole preparation is as
EXPERIMENTAL
follows. A hot (100–130°C) solution of catalyst, a
mixture of complex IV with oxime III, prepared from
NaOH and oxime III in DMSO (by removal of water
as azeotrope with toluene) is added in a nitrogen flow
to a hot (100–130°C) DMSO purged with nitrogen for
removal of oxygen and carbon dioxide. The preferable
concentrations of the components in the reaction
Four liters of DMSO and 1.75 L of a catalyst soluꢀ
tion obtained from 750 g of oxime III, 50 g of NaOH
0.87% of reaction mixture weight), and 1 L of DMSO
using toluene as an azeotropic agent) were placed into
a steel reactor (10 L) equipped with a mechanical stirꢀ
rer, electrical heating jacket, and internal cooling coil.
Nitrogen was passed through the reaction mixture on
heating (120–130°C) and with stirring for 0.5 h at a
rate of 0.8–1.0 L/min, then acetylene was passed at a
rate of 1.25–1.50 L/min (acetylene outlet flow rate is
(
(
mixture (catalyst solution) are 13–17% of oxime III
,
0.5–1.5% of NaOH. Acetylene is passed through the
reaction mixture at 120–130°C at a rate that provides
about 95% conversion. Acetylene supply is terminated
when conversion of oxime III reaches 70–80%. The
reaction mixture is kept at 100–130°C for 0.5–1 h
until dissolved acetylene reacts completely, purged
1
25–150 mL/min, acetylene conversion is 90%) durꢀ
ing 2.5 h. Temperature in the reactor (125–130°C)
was adjusted by varying the rate of acetylene supply
and internal cooling (cold water was passed through
the coil to compensate for exothermic effect). After
completion of acetylene passage, the reaction mixture
was kept for another 0.5 h at 120–130°C and treated
with nitrogen, neutralized (CO ), and vacuum disꢀ
2
tilled. First, 80–90% of DMSO is distilled off (which
can be reused in the process after azeotropic drying
with toluene). Then, the crude product containing
as noted above to give 544 g of indole
oxime III (conversion is 71%). The yield of
with respect to reacted oxime III, purity of 99%
admixture of II is 1%).
I
and 220 g of
DMSO (30–50%), indole
10–20%) is vigorously stirred with an equal volume of
toluene and a 10–20% aqueous solution of NaOH
0.2–0.4 of the fraction volume). The aqueous alkaꢀ
I (30–40%), and oxime III
I
was 96%
(
(
(
line phase is separated, a new portion of aqueous
NaOH is added (0.1–0.2 of the toluene layer volume),
and extraction is repeated. Extraction process comꢀ
pletes when only trace amount of oxime III is detected
ACKNOWLEDGMENTS
This work was supported by the Council for Grants
in the toluene layer. Toluene is distilled off from the of the President of the Russian Federation for State
toluene layer, this is accompanied by simultaneous Support of Leading Scientific Schools (grant no. NSh
azeotropic drying of indole
tion residue. Vacuum distillation of the residue affords
pure indole in 95–97% yield at the conversion of
oxime III of 70–90%. Water is distilled off from the
aqueous alkaline extracts, while the residue containing
DMSO, NaOH, and sodium cyclohexanone oximate
as a complex with DMSO can be further used for the
preparation of catalyst solution.
I
remaining in the distillaꢀ 3230ꢀ010.3).
I
REFERENCES
1
. Sundberg, R.J., The Chemistry of Indoles, San Diego:
Academic, 1997.
2
. Madsen, J.Ø., Meldal, M., Mortensen, S., and
Olsson, B., Acta Chem. Scand. B, 1981, vol. 35, no. 2,
pp. 77–81.
Thus, we have developed a new industrially conveꢀ
nient technology for the synthesis of 4,5,6,7ꢀtetrahyꢀ
droindole from cyclohexanone oxime and acetylene
3
. Trofimov, B.A. and Mikhaleva, A.I., NꢀVinilpirroly
(NꢀVinylprroles), Novosibirsk: Nauka, 1984.
DOKLADY CHEMISTRY Vol. 435
Part 1
2010