SYNTHESIS OF ENERGETIC COMPOUNDS
313
rent of 50 µA) on a 70000 × 0.25-mm capillary column compound IV, 89.69 wt %; unidentified impurities,
coated with Apiezon L, as well as with a Kratos instru- 0.26. During the reaction, which lasted 2 h, ethylene
ment on a 2000 × 3-mm column packed with 3% SE-30- was released. According to GLC data, liquid products
coated Chromaton). The proton NMR spectra were contained unreacted compounds IV and I, as well as
recorded on a JEOL (100 MHz) instrument. The IR dicyclobutylidene resulting from metathesis, product
spectra were recorded with a Specord spectrophotome- III, and its isomers. The yield of diene III and its iso-
ter in a 5% CCI4 solution, as well as in the solvent-free mers calculated on the basis of reactant I fed was
mode.
21.63 mol % and that calculated on the basis of reactant
I converted was 78.16 mol %. The yield of dicyclobu-
tylidene calculated on the basis of reactant IV fed was
17.37 mol %, and the selectivity for dicyclobutylidene
was 78.92 mol %.
Transformations of Methylenespiro[2,3]hexane (I)
on Promoted Rhenium–Alumina Catalysts
The rhenium–alumina catalyst was prepared
according to the conventional procedure [2]. The reac-
tion was carried out at 35°ë in a thermostated batch
reactor equipped with a stirrer. A catalyst (0.78 g) pre-
liminary activated at 580°ë in a flow of air for 1 h and
in a flow of nitrogen for 1 h was placed into the reactor.
After thermostating, the catalyst was promoted with
1.3 wt % tetraethyl lead. Then, 3.9 ml (3.1 g) of com-
pound I cleaned of acetylenic compounds was added.
The reaction was accompanied by heat evolution. After
2 h, according to GLC data (SE-30, l = 3 m), the reac-
tion mixture had the following composition (wt %):
unreacted I, 53.88; diene III and its isomers, 38.86; and
unidentified hydrocarbons, about 7.26. The yield of
diene III and its isomers calculated in terms of reactant
I taken was 39.25 mol %, and the selectivity of the con-
version of I into these products was 86.13 mol %. Prod-
uct III was isolated by preparative chromatography
with a purity of 97 wt % (a PEG 1000 column; l = 3 m;
and column and evaporator temperatures of 200 and
200°ë, respectively). The structure of III and its physi-
cochemical and spectral characteristics are given in the
table. A mixture of the isomers of III was isolated with
a purity of 95 wt %. The IR, 1H NMR, and mass spec-
tral data for diene III are given in the table.
Synthesis of 4-Cyclobutylidenespiro[2,3]hexane
The 10% Re2O7/Al2O3 catalyst activated in a nitro-
gen flow at 580°C was placed into a reactor similar to
the one described above. After cooling, the catalyst was
promoted with tetraethyl lead (1.3 wt %). The reactor
was thermostated at 35°ë, and a mixture of I (14.73 wt %)
with dicyclobutylidene (83.56 wt %) was added to the
reactor. The reaction was run at a constant temperature
of 35°ë with stirring for 2 h. Neither gas emission nor
heat evolution was observed. According to GLC data,
the resultant mixture contained unreacted compound I,
dicyclobutylidene; compounds IV and IX as comet-
athesis products; and unidentified hydrocarbon impuri-
ties. The yield of IX on a fed reactant I basis was
45.29 mol %, the selectivity of the transformation of I
was 96 mol %. The yield of IX on the fed dicyclobutyl-
idene basis was 100 mol %. The desired product
4-cyclobutylidenespiro[2,3]hexane was isolated to
have a 97 wt % purity via vacuum rectification followed
by preparative chromatography under the aforemen-
tioned conditions. Its physicochemical and spectral
characteristics are given in the table. The kinetics of the
cometathesis reaction of compound I with dicyclobu-
tylidene is illustrated in the figure.
Transformation of a Mixture of I and IV
REFERENCES
on PbEt4-Promoted Rhenium–Alumina Catalyst
1. Houben-Weyl. Methoden der organischen Chemie
(Georg Thieme, Stuttgart, 1953; Khimiya, Moscow,
1967).
The reaction was carried out at 35°ë in a batch sys-
tem composed of a thermostated reactor equipped with
a stirrer and an arrangement for the withdrawal of the
ethylene produced. The 10% Re2O7/Al2O3 catalyst acti-
vated at 580°ë was loaded into the reactor and pro-
moted with tetraethyl lead (1.3 wt %) after cooling.
Then, a mixture of I and IV was added. The mixture had
the following composition (wt %): compound I, 10.05;
2. E. Sh. Finkel’shtein, B. S. Strel’chik, S. V. Kotov, et al.,
Neftekhimiya 25, 41 (1985).
3. B. A. Dolgoplosk, K. L. Makovetskii, and E. I. Tinyak-
ova, Dokl. Akad. Nauk SSSR 228, 1109 (1976).
4. B. A. Dolgoplosk, E. I. Tinyakova, and V. A. Yakovlev,
Dokl. Akad. Nauk SSSR 232, 1075 (1977).
PETROLEUM CHEMISTRY Vol. 48 No. 4 2008