REACTIONS OF C H O WITH C H O AND O
3
69
6
5
6
5
Ϫ
3
cm , respectively, the phenoxy recovery time from
rex injector that was concentric with the reactor tube.
The observed first-order decay rate was corrected for
axial diffusion and for loss of C H O on the injector
Ϫ4
reaction 6 is about 10 s, which is three orders of
magnitude faster than its consumption time estimated
from reaction 7), the Cl atom formed in reaction 7
would be titrated completely and essentially immedi-
6
5
according to eq. [II] [18,19]:
ately, and the C H O radical loss due to reaction 7 was
2
6
5
kЈ ϭ kЈ(1 ϩ kЈD/v ) ϩ k
[II]
corr
p
quickly regained by reaction 6. Therefore, the inter-
ference of reaction 7 on the kinetic measurement of
phenoxy radical self-reaction can be neglected.
where D is the diffusion coefficient, v is the mean bulk
flow velocity and k is the first-order loss of C H O on
the surface of the sliding injector. The diffusion co-
p
6
5
Buth et al. measured the rate constant of phenoxy
radical self-reaction indirectly by competing the
C H O ϩ O reaction with the C H O ϩ C H O reac-
efficient D for C H O in the helium was estimated
6
5
6
5
6
5
6
5
based on the empirical equation developed by Fuller
tion. They reported a rate constant of k ϭ (3.32 ϩ
2
1
et al. [23], which yielded approximately 0.30 atm cm
s
Ϫ11
3
Ϫ1
Ϫ1
3
.32/Ϫ1.66) ϫ 10
cm molecule
s
[13]. Re-
Ϫ1
at 298 K. The corrections for axial diffusion were
cently, Berho et al. determined the rate coefficient for
always less than 1%. Finally, the bimolecular rate con-
Ϫ
11
the C H O self-reaction to be (1.22 Ϯ 0.02) ϫ 10
6
5
stant for reaction 2, k , was obtained from slopes of
2
3
Ϫ1
Ϫ1
cm molecule
with UV absorption spectrometry at 1 atm and 298 K
the error bar was later modified to be Ϯ 0.24) [17].
Our rate constant value for reaction 1 (k ϭ (1.49 Ϯ
s
using a flash photolysis coupled
linear least-squares fits to the plots of kЈcorr vs. the ex-
cess reactant concentration.
The determination of absolute concentration of O3
is important in measuring the rate constant for reaction
(
1
Ϫ11
3
Ϫ1
Ϫ1
0
.53) ϫ 10 cm molecule s ) is in good agree-
2
. In this work, O measurement was calibrated by the
3
ment with that measured by Berho et al., but is about
a factor of two lower than that reported by Buth et al.
The loss of the C H O on the wall was suggested
chemical conversion of O to NO by reacting O with
3
2
3
excess of NO:
O ϩ NO !: NO ϩ O
2
6
5
to contribute to the large uncertainty in Buth et al.’s
measurement [13]. In our experiment, however, no
significant decrease of the C H O signal was observed
3
2
Ϫ14
3
Ϫ1
Ϫ1
k8 ϭ 1.8 ϫ 10
cm molecule
s
[22] (8)
6
5
when the radical was introduced to the reactor from
the side arm and exposed to the sliding injector sur-
face, indicating a negligible, if any, loss of the C H O
This was accomplished by introducing NO from the
sliding injector and O from the side arm of the reactor
6
5
3
onto the Pyrex wall. The coverage of a Teflon sheet
to the internal surface of the reactor should further help
in reducing the wall loss of the phenoxy radical. Thus
the contribution of the wall loss to the C H O decay
tube, with the injector placed in a downstream position
to minimize the further reaction of NO with O . The
conversion factor was determined from the ratio of the
2
3
change in O signal (m/e ϭ 48) to that of NO (m/e ϭ
6
5
3
2
in our C H O self-reaction rate constant determination
46), which yielded ⌬S /⌬S ϭ 0.49. Then the ab-
6
5
48 46
should be negligible.
solute calibration of the mass spectra signal at m/e ϭ
6 allowed the evaluation of the absolute O concen-
4
3
tration.
Figure 3 shows the corrected pseudo-first-order de-
cay rate, kЈcorr, as a function of O concentration. With
Phenoxy Radical Reaction with Ozone
Kinetic measurement for reaction 2 was carried out by
monitoring the decay of phenoxy radical as a function
of reaction time in the presence of ozone. The rate
constant for this reaction was obtained using the well-
known steady-state flow-tube method [18–21]. Fol-
lowing this method, the experiments were carried out
under pseudo-first-order conditions, in which the con-
centration of O was in excess over that of C H O.
3
1
1
initial C H O concentrations of (3.30–10.4) ϫ 10
6
5
Ϫ
3
molecule cm and O3 concentrations of (1.45–
1
3
Ϫ3
11.0) ϫ 10 molecule cm , kЈ varies from 7 to 33
corr
Ϫ
1
s . The slope of the linear least-squares fit through all
the data yields k ϭ (2.86 Ϯ 0.35) ϫ 10 cm mol-
Ϫ
13
3
2
Ϫ1
Ϫ1
ecule
s
for the reaction of C H O with O , where
6 5 3
the quoted uncertainty corresponds to 2. The rapid
self-reaction of the phenoxy radical may add compli-
cation to this measurement. Because the C H O was
3
6
5
The pseudo-first-order decay rate, kЈ, was determined
from slopes of plots of the logarithm of phenoxy rad-
ical concentration against injector distance, which de-
termined the contact time of the reactants. In these
experiments C H O was introduced into the flow tube
6
5
introduced from the side arm, there may be a C H O
6
5
concentration gradient going from the upstream to the
downstream of the reactor. This potential effect was
reduced by taking the C H O decay data within the
6
5
as a minor reactant through a fixed side arm, and the
6
5
excess reagent, O , was added through the sliding Py-
first 20 ms contact time domain, which was less than
3