8840 J. Phys. Chem. A, Vol. 101, No. 47, 1997
Park et al.
trace amount of C6H6. Addition of H2 to the system noticeably
reduced the yields of C12H10 and C6H5CH3, with a concomitant
increase in the yield of C6H6. Table 2 summarizes the
experimental conditions employed and the yields of C6H6 and
C6H5CH3 measured in the PLP/MS experiment. Kinetic model-
ing of the absolute concentrations of these products, determined
by careful calibrations using standard mixtures sampled at the
same total pressure employed in each run, gave the rate constants
for the formation of C6H6 and C6H5CH3 by the following
respective reaction:
C H + H f C H + H
6
5
2
6
6
C H + CH f C H CH
3
6
5
3
6
5
CH4 is present in these experiments in a much lower concentra-
tion than C6H6 and was presumed to be formed by the CH3 +
H2 f CH4 + H reaction. The comparison of the measured
and predicted yields will be discussed in the following section.
6 5 6 6
Figure 2. Time-resolved C H NO decay (solid points) and C H
formation (open circles) profiles in P/FTIR experiments at T ) 598 K.
Lines are the modeled results. Reaction conditions are given in Table
1
.
III. Results and Discussion
a
TABLE 1: Experimental Conditions and Modeled Rate
Constants in P/FTIR Experiment for the Reaction of C
at Temperatures Studied
1
. Kinetics of the C6H5 + H2 Reaction. The rate constant
6
5
H +
H
2
of the C6H5 + H2 reaction can be obtained by kinetic modeling
in a straightforward manner. The mechanisms employed for
the modeling are presented in Tables 3 and 4 for the pyrolysis
of C6H5NO-H2 mixtures and the photolysis of C6H5COCH3-
H2 mixtures, respectively.
3
(cm /mol‚sec)b
T (K) [C NO] [Ar]
6
H
5
0
0
[H
2
]
0
k
4
-
8
8
8
8
8
8
8
8
-5
-5
-5
-5
-5
-5
-5
-5
-5
-5
-5
-5
-5
-6
-6
-6
8
5
5
5
5
5
5
5
6
48 1.70 × 10
0.00 × 10
1.17 × 10
1.04 × 10
1.02 × 10
1.00 × 10
1.10 × 10
1.09 × 10
1.07 × 10
2.22 × 10
1.02 × 10
1.13 × 10
1.11 × 10
1.09 × 10
9.64 × 10
9.49 × 10
9.35 × 10
7.45 × 10
-
-
-
-
-
-
-
9
58 1.43 × 10
63 1.58 × 10
73 1.55 × 10
83 1.53 × 10
89 1.35 × 10
98 1.33 × 10
07 1.31 × 10
(1.18 ( 0.66) × 10
9
1.14 × 10
9
9
9
9
9
(1.20 ( 0.18) × 10
(1.44 ( 0.15) × 10
(1.35 ( 0.14) × 10
(1.48 ( 0.20) × 10
(1.99 ( 0.13) × 10
In the thermally initiated C6H5NO and H2 reaction, the
formation of C6H6 was influenced by the following primary
processes:
C H NO ) C H + NO
(1, -1)
(2)
6
5
6
5
a
3
b
The concentration units are in mol/cm . For each temperature
except 548 and 563 K), typically 3-5 runs were carried out. The
(
C H + C H f C H
6 5 6 5 12 10
uncertainty represents 1σ.
C H + C H NO f C H NO
(3)
major absorption peaks of the reactant and product are clearly
separated. The C6H6 peak at 673.1 cm overlaps with a small
peak of C6H5NO; the overlap can be readily corrected. Figure
6
5
6
5
12 10
C H + H f C H + H
(4)
6
5
2
6
6
2
shows a typical set of the concentration vs time plots for the
All but reaction 4 have been determined recently by us.16,26 The
results of our sensitivity analysis (see Figure 3) bear this out.
In order to account for the loss of C6H5, several secondary and
tertiary reactions were included in the modeling, employing
formation of C6H6 and the decay of C6H6NO. The correspond-
ing curves represent kinetically modeled values. The values
of the rate constant for C6H5 + H2 obtained by modeling are
summarized in Table 1. The mechanism employed for modeling
will be discussed later.
“
reasonably” assumed values of radical-radical reaction rate
constants (see Table 3). The values of rate constant for the
C6H5 + H2 reaction are presented in Table 1 and Figure 5 (vide
infra).
2. PLP/MS. By the mass-spectrometric method, the pulsed
photolysis of C6H5COCH3 at 193 nm was employed as the C6H5
radical source. C6H5COCH3, carried by an excess amount of
He was premixed in corrugated stainless steel tubing with H2
In the photoinitiated reaction of C6H5COCH3 in the presence
of excess amounts of H2, the production of C6H6 was found to
be influenced by the following primary processes:
2
7,28
before being introduced in the Saalfeld-type quartz reactor
which can be heated to 1200 K. The reactants and the products
of the photoinitiated reaction were supersonically sampled and
ionized by electron-impact ionization. The mole fraction of
C6H5COCH3 was typically <0.5% and that of H2 >75%, with
C H + C H f C H
12 10
(2)
(4)
(5)
(6)
6
5
6
5
C H + H f C H + H
6
5
2
6
6
[H2]/[C6H5COCH3 ] > 150. The conversion of C6H5COCH3
by the unfocused ArF laser beam ranged from 15% to 40%.
The mechanism for the fragmentation of C6H5COCH3 at 193
nm has been studied by using NO or HBr as the C6H5 radical
scavengers.29 The kinetic modeling of measured yields of C6H5-
NO or C6H6 and CH4 under fully inhibited conditions revealed
that ∼80% of the fragmentation reaction gave rise to C6H5. This
result is consistent with the measured yield of C6H5CH3 without
NO or HBr. The introduction of an excess amount of NO, for
example, eliminated the formation of toluene.29
C H + CH f C H CH
3
6
5
3
6
5
CH + CH f C H
6
3
3
2
The result of sensitivity analysis carried out at 887 K (see Figure
4) clearly bears this out. Again, in order to minimize the loss
of C6H5 in our simulation, several secondary and tertiary
reactions were included in the model as shown in Table 4. A
sensitivity analysis of this system shown in Figure 4 reveals
that the yield of C6H6 is most strongly and positively affected
by reaction 4 and negatively influenced by its competitive
reactions 2 and 5.
In the absence of H2, the major molecular products from the
C6H5COCH3 photolysis were C6H5CH3, C2H6 and C12H10
(which was not quantitatively determined in this study), with a