SYNTHESIS OF 8-ACETOXYTETRACYCLO[4.4.12.5.17.10.01.6]DODEC-3-ENE
1663
Scheme 2.
O
3
3
O_C_R
11
7
11
7
15
4
1
O
O
4
2H
2
10
10
6
1
9
9
cat
_
_
CH3 C_O
+
R_COOH
CH3 C_O
12
12
5
13
14
5
13
14
8
H
8
6
H
I
II_VII
VIII_XIII
R = H (II), CH3 (III), CH3CH2 (IV), (CH3)2CH (V), CH3(CH2)2 (VI), C4H9 (VII).
All three stages of the reaction simultaneously
proceed in a pressure reactor. The effect of tem-
perature, of molar ratio of components, of the reaction
time, and of the amount of nano-TiO2 catalyst on the
yield of compound I was studied, and optimal param-
eters of synthetic procedure for the target product were
evaluated. It was shown that optimum parameters of
synthesis areas follows: tricyclo[5.2.1.02.6]deca-3,8-
diene : vinyl acetate molar ratio 1 : 1–1.25 wt % of
nano-TiO2 catalyst, 0.2 mass % of hydroquinone with
respect to tricyclo[5.2.1.02.6]deca-3,8-diene, tempera-
ture 190°C, and the reaction time 4 h. After filtering of
the heterogenic catalyst and distillation in a vacuum
the target product I was obtained in 88.5% yield.
90°C the yield of tetracyclododecan-3,8-diol diacetate
IX increases from 52.5 to 70.0%. Further increase in
temperature to 120°C causes the decrease in the yield
of compound IX to 50.0% due to the formation of side
products of dimerization and oligomerization of the
starting substance I. Therefore 90°C was accepted as
the optimum reaction temperature (see Fig. 1a).
The dependence of the target product yield on the
I : III reagent ratio was studied in the range 1 : (1–1.5)
(see Fig. 1b). Experiments were carried out at 90°C for
3 h using 0.2 wt % of catalyst. The yield of diester IX
grows from 45.5 to 76.0% at the increase of reagent
ratio from 1 : 1 to 1 : 1.3. Further increase to 1.5 mol
decreases the yield of the target product to 73.2%.
The composition and purity of the synthesized
unsaturated tetracyclic monoesters were evaluated by
means of GLC. It was shown that monoester is a
mixture of 28.0% of endo-endo- and 72% of exo-exo-
steric isomers.
The influence of the catalyst amount was studied at
the above-established optimum values of the
temperature and reagent ratio and the reaction time 3 h
(see Fig. 1c). Amount of catalyst was varied in the
range 0.4–0.6 wt %. The use of 0.5 wt % of catalyst
was optimal, because the yield increased from 60% to
79%. Using larger amount of the boron trifluoride
etherate decreased the target product yield to 56.5%.
The product obtained was heated at 200°C for 1 h
to carry out isomerization of the mixture to most stable
exo-exo-isomer [7]. This process resulted in the
formation of monoester containing 99.9% of exo-exo-
and 0.1% of endo-endo- isomer.
Yield of compound IX depends also significantly
on the reaction time (see Fig. 1d). Its increase from
1 to 4 h permits to achieve 90% yield of diacetate, but
more prolonged heating decreases the yield of
compound IX to 85%.
In the second step of our work the synthesis of
diesters by catalytic addition of saturated C1-C5
monobasic acids to cycloalkene I was investigated.
Boron trifluoride etherate as catalyst was used. The
reaction can be described by the Scheme 2.
Hence, optimal parameters of diacetate IX forma-
tion in the reaction of compound I with the acetic acid
III in the presence of boron trifluoride etherate are as
follows: reaction temperature 90°C, molar ratio of com-
pounds I and III 1 : 1.3, amount of the catalyst 0.5 wt %
with respect to substance I, reaction time 4 h. Under
optimum conditions yield of product IX reaches 90%.
Addition of formic II, propionic IV, butyric V,
isobutyric VI, and n-valeric VII acids was carried out
analogously. Yields of the products, their physico-
chemical characteristic, and elemental analysis data are
listed in Table 1.
By an example of acetic acid the effect of
temperature, of molar ratio of the reaction components,
of the amount of catalyst, and of the reaction time on
the yield of tetracyclo[4.4.12.5.17.10.01.6]dodecan-3.8-
diol diacetate IX was studied.
I : III molar ratio 1 : 1, 0.2 wt % of catalyst and the
reaction time 3 h were used as starting conditions. The
temperature of the reaction was varied with in the limits
70–120°C. At the increase in temperature from 70 to
RUSSIAN JOURNAL OF GENERAL CHEMISTRY Vol. 84 No. 9 2014