Oligomerization of oxadiazole derivatives
Russ.Chem.Bull., Int.Ed., Vol. 62, No. 6, June, 2013
1439
release rate of the initial compound I. Therefore, the iniꢀ
tial region of heat release rate characterizes the reactivity
of intrinsic oxadiazole I. It also could be assumed that the
initial region is related to the equilibrium transformation
of one conformation of the substance into another. Howꢀ
ever, experiment at 170.5 С with interrupting of the reacꢀ
tion at the minimum of the heat release rate and cooling of
the sample to ~20 C with the purpose to shift the conforꢀ
mational equilibrium to the initial position followed by
the repeated placing the ampule into the calorimeter to
continue the reaction did not confirm this assumption.
After the ampule was heated, the same heat release rate
that was observed before interrupting experiment was deꢀ
tected. The regular decrease in the rate at the initial region
at the lowest boundary of the temperature range (176.1 C)
was observed within 75 min and at the upper boundary
(201.6 С) within 20 min. Additional studies are needed to
reveal a reason for such a decrease in the rate.
Assuming that the isomerization of oxadiazole I to the
imidazole derivative followed by oligomerization to form
the polyimidazole derivative as the major reaction that
explains the observed thermal effect of the reaction,
the kinetic scheme of the process will consist of the folꢀ
lowing stages.
(1) Chain generation:
— 1,2,4ꢀoxadiazole derivative transforms into the imidꢀ
azolol derivative;
plex of constants of oligomerization stages, the depenꢀ
dence of the specific reaction rate (d/dt)/(1 –)1.5 on
the reaction depth was analyzed:
,
where d/dt = (dQ/dt)/Q0 is the process rate, and (dQ/dt)
is the heat release rate (Fig. 5).
The formation of oligomer already at small depths of
conversion increases the viscosity of the reaction medium
and, as a consequence, decreases the termination rate conꢀ
stant, which is limited by the diffusion rate of oligomer
radicals. As a result, the oligomerization rate increases in
the range of 1—20% reaction depth. At high depths of
conversion, an increase in the viscosity of the system reꢀ
sults in the situation where the rate of monomer diffusion
to the oligomer radical becomes the rateꢀdetermining step
for the chain propagation reaction, which formally leads
to a decrease in the chain propagation rate constant and,
finally, to a decrease in the ratio of the chain propagation
rate constant to the square root of the chain termination
rate constant. The oligomerization rate constant deterꢀ
mined by this ratio and the monomer concentration also
begins to decreases from a certain depth of conversion.
The experiment at 192.3 С in which an equal weight
of the oligomer reaction products was added to the startꢀ
ing compound I confirms the conclusion about the subꢀ
stantial influence of the viscosity of the reaction medium
on the polymerization rate (Fig. 6). The addition of the
product increases the initial heat release rate by 3.7 times.
Then the rate only decreases during the process. The heat
of the thermal transformation of oxadiazole I in the presꢀ
ence of the reaction product does not differ from that for
the thermal transformation of the pure compound.
— cleavage of the imidazole ring at the ordinary N—C
bond to form the biradical.
(2) Chain propagation:
— interaction of the biradical with the free valence on
the nitrogen atom with the C=N double bond of the imidꢀ
azole ring results in the formation of the free valence on
the C atom of the heterocycle and an increase in the biradꢀ
ical length by one structural unit;
— similar chain generation reactions occurs beginning
from another end of the biradical with the free valence at
the C atom.
The degree of acceleration remains almost unchanged
when the ratio of the weighed sample to the free volume of
(d/dt)/(1 – )1.5
(3) Chain termination:
— reactions of closure of macrobiradical end with free
valences at the nitrogen and carbon atoms to form macroꢀ
cycles with N—C, N—N, and C—С bonds. These reacꢀ
tions lead to the formation of a network (crossꢀlinked)
polymer. An increase in viscosity decreases the probability
of collision of the biradical ends to form the macrocycle,
which corresponds to a decrease in the chain termination
rate constant and results in the observed increase in the
rate of oligomerization of the starting compound.
The observed dependence of the heat release rate on
the reaction depth is determined by both the change in the
monomer concentration in the course of the process and
the change in the chain termination rate constants due to
an increase in the viscosity of the reaction mixture when
oligomer molecules are formed. To distinguish the influꢀ
ence of the increasing viscosity of the medium on a comꢀ
0.5
0.4
0.3
0.2
0.1
0.2
0.4
0.6
0.8
1.0
Fig. 5. Oligomerization rate of compound I (d/dt)/(1 –)1.5 vs
reaction conversion at 192.3 С.