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N Sharath et al.
above step is formed in the decomposition of 3-carene, isoprene decomposition showed the formation of allene,
transition state structure for the above reaction is also we are proposing the following reaction to explain the
given in the figure 5(g). A schematic diagram show- formation of xylene.
ing relative energies of reactant, intermediates and tran-
sition states with respect to isoprene energy has been
[R26] C5H7 + C3H4 = C8H10 + H
Reactions R17 and R18 were included to check
whether xylene could be a secondary product formed
by reaction of toluene and CH3 radical. For Reaction
R17, a range of rate constants in the literature were also
considered. The rate constant for the reaction was var-
ied in the available data range to find out its effect on
xylene formation. The recombination rate constant for
R19 was approximated to the following reaction.
3.3 Kinetic Mechanism
With the help of results described in experimental and
theoretical sections, the mechanism for the 3-carene
thermal decomposition given in table S2, with 44
reactions involving 37 species, has been derived to fit
the product concentrations observed in the present ex-
perimental work. Since a mechanism for pyrolysis of
both 3-carene and isoprene does not exist in the litera-
ture, we have tried to use minimum number of reactions
to explain the product profiles observed in the present
experiments.
After simulating the mechanism, given in table S2, at
reaction conditions given in table 1, it was again simula-
ted at 300 K and 2 atm for 10 ms. This has been done
to take into account of radical reactions which can con-
tinue until all are consumed. The rate parameters used
in the mechanism are obtained from TST calculations
and refined to fit the observed concentrations. For sim-
ple molecular systems, such refinements in TST rate
parameters may not be required. However in the present
case, even with such a detailed analysis for the consid-
ered system we could not explain the observed prod-
uct concentrations without such small variations in
the calculated theoretical rate parameters. To compare
the rate parameters calculated using TST at B3LYP/6-
311+G(d,p) level of theory and the one used in the
mechanism, the former is also given in table S3.
The rate constant for reaction R9 was obtained using
the literature and the present work. Pre-exponential fac-
tor was obtained using the variational transition state
theory and the activation energy was obtained using
reported work.34 The pre-exponential factor for R14
was increased from 6.16 × 1011 to 1.00 × 1012 cm3
mole−1 s−1. The Arrhenius rate parameters, 9.77 ×
1012 cm3 mole−1 s−1 and 0.1 kcal mol−1 given in the
literature35 for reaction R16 can be compared with
present values of 6.0 × 1014 cm3 mole−1 s−1 and 0.1
kcal mol−1. The n factor used the literature for R16 is -
0.08 while in the present work we have used n factor of
0.7 for the same.
[R25] C6H5 + CH3 = C6H5CH3
The obtained results suggested that the reactions R17
and R18 will not be able to explain xylene concentration
obtained in the present experimental work. Thus, xylene
could have formed through reaction R26. Rate constant
for the above reaction was fitted to obtain the observed
xylene concentration. One more possible pathway for
xylene formation could be that of C4H5 dimerisa-
tion process, but, it is not considered in the present
work. The comparison of concentrations obtained in
experiments and simulation is given in figure 13 and the
results are in reasonable agreement.
4. Conclusions
Thermal decomposition experiments of 3-carene have
been carried out for temperatures ranging from 920 to
1220 K. Linear products were found to form in major
concentrations. Ab initio calculations were carried out
to help in deriving and understanding the pyrolysis
mechanism of 3-carene. Opening of C3 ring in 3-carene
as well as in C10H15(A) and C10H15(B) was found to be
the first step in their decomposition process. Theoreti-
cal calculations also showed that 3-carene decomposi-
tion will lead to the formation of linear products. Rate
parameters obtained using transition state theory was
refined and used in the kinetic mechanism presented
in the paper. The mechanism fairly replicated the for-
mation of observed product concentration. This is the
first detailed experimental and theoretical work carried
out on 3-carene decomposition process. We hope that
this work will help in deriving the oxidation mecha-
nism and, stimulate further experimental and theoretical
studies on the pyrolysis of this important molecule.
Pre-exponential factor for R25 was increased from
1.38 × 1013 to 6.0 × 1013 cm3 mole−1 s−1. We are
unable to explain xylene formation through transition
Supplementary Information
state theory. Since isoprene decomposition also resulted Full citation for Ref 27., sensitivity of FID to the
in the formation of xylene, and, previous results of molecules, tables S1-S6, selected potential energy