2
666 J. Phys. Chem. A, Vol. 103, No. 15, 1999
Tokuhashi et al.
been carried out using a He carrier). The region between the
flash lamp (or excimer laser for the LP method) and the reaction
cell is purged with dry N2.
reactor was maintained either by electric heater (298-430 K),
or by circulating heated water (298-339 K) and cooled
ethanol-water mixture (250-273 K) in the outer jacket of the
reaction cell from a thermostated bath. It was measured by CA
thermocouple at the top of the inner tube of the sliding injector
Water vapor was supplied by bubbling a certain part of carrier
gas through a vessel filled with water at room temperature. The
total pressure of carrier gas containing water vapor was
measured by a capacitance manometer, and was kept constant
by a control valve. The amount of water vapor supplied to the
reaction cell was estimated from the flow rate of the carrier
gas, water temperature measured by CA thermocouple (type
K), and total pressure of carrier gas containing water vapor. To
prevent accumulation of photofragments or reaction products
in the cell, all photolysis experiments were carried out under
slow flow conditions. For both LP and FP methods, initial
concentration of OH radicals, which is estimated from com-
parison with fluorescence intensities obtained with the DF
(for the DF method) or at the spot around 1-2 cm downstream
from the probe laser beam (for LP and FP methods). During
the experiments, the temperature across the reaction volume was
maintained better than (2 K over the temperature range
examined. The gas flow rates, the total pressure, and the reaction
temperature were monitored by the second computer through a
digital recorder or data acquisition controller, and stored in a
computer via RS-232C circuit. To ensure that the experimental
data are free from any systematic errors, the experiments were
repeated at intervals from several days to several months under
a variety of flow conditions.
method, is always kept smaller than 1011 molecule cm-3. The
repetition rate of the photolysis light was set as 10 Hz.
Sample Analysis and Purification. The samples of fluori-
nated alcohols were analyzed by using gas chromatography with
an FID detector, where the area ratio of main peak against total
area was taken as the purity of the sample. The analytical
columns used in the present work are G-205 (1.2 mm i.d., 40
m long, film thickness 5 µm, Chemicals Inspection & Testing
Institute, Japan, He carrier gas), or stainless steel column (3
mm i.d., 10 m long) packed with mainly Silicone DC 702
A primary carrier gas, He (99.995%) or Ar (99.995%) was
used without further purification. N2O (99.999%) diluted with
He was purchased as a mixture with N2O concentration of
around 1%.
Laser-Induced Fluorescence Method. The concentration of
OH radicals has been measured by the LIF method. In the case
of DF and FP methods, the apparatus is the same as that for the
LP method shown in Figure 2. The excitation light is from a
frequency-doubled tunable dye laser (Spectron, SL4000B), and
the wavelength was tuned at about 308 nm. The dye laser was
pumped by pulsed light of a frequency-doubled Nd:YAG laser
(Shimadzu, N2 carrier gas). The lower value obtained using two
columns was taken as a purity of the sample. The purities of
CF3CH2OH and CF3CH(OH)CF3 samples were found to be
9
9.994 and 99.999%, respectively, and these samples were used
without further purification. The sample of CF3CF2CH2OH
99.56%) was purified by gas chromatography. In the purifica-
(
(Spectron, SL803). The repetition rate of the laser was set as
tion process, the vapor of CF3CF2CH2OH was charged in an
10 Hz. Fluorescence signals due to OH radicals were monitored
3
evacuated sampling tube (inner volume of about 50 cm ), and
at a right angle against both the excitation light and the
photolysis light (or flow tube for the DF method), and focused
by quartz lenses and a concave mirror, and detected by a
photomultiplier tube. The scattered light of the excitation light
supplied to a stainless steel column (9.6 mm i.d., 4 m long)
packed with Silicone DC 702 through a six-way switching
cock. Nitrogen was used as the carrier gas. The middle frac-
tion of the main peak (chromatogram was always monitored
by TCD detector) was collected through a four-way switching
cock into a trap cooled with liquid nitrogen. The sample of
CF3CF2CH2OH thus obtained showed purity of 99.935%.
(
and photolysis light source for LP and FP methods) was
reduced by a monochromator (Jarrell-Ash, Monospec 25,
360G/mm, 25 cm focal length). The output signal of the
2
photomultiplier tube was amplified by a preamplifier, and
accumulated (usually 400-600 shots) by a multichannel scaler/
averager (Stanford, SR430), or averaged (usually 128 shots by
a digital storage oscilloscope Gould-4050), and stored in a
microcomputer for further data processing. Trigger pulses for
YAG laser, multichannel scaler/averager (or digital storage
oscilloscope), and photolysis light source were generated by a
delay generator (Stanford, DG535). This computer was used to
control the delay generator (for LP and FP methods), pulse
controller (to determine the position of sliding injector for DF
method), and the other computer (see later).
Results and Discussion
According to the gas chromatographic analysis made before
the kinetic measurement, the purities of the samples of
fluorinated alcohols as supplied are 99.994, 99.56, and 99.999%
for CF CH OH, CF CF CH OH, and CF CH(OH)CF , respec-
3
2
3
2
2
3
3
tively. The individual impurities were not characterized though.
At any rate, since the impurity levels of CF CH OH and
3
2
CF CH(OH)CF in particular are extremely low, it is obvious
3
3
that the effects of impurities on the measurement of the OH
rate constants may be negligibly small for these samples. We
began with measuring the OH reaction rate constant for
CF3CH2OH and CF3CH(OH)CF3.
Gas Handling and Measurements. Various gas flow rates
were measured and controlled by calibrated mass flow control-
lers. In particular, the flow rate of fluorinated alcohol vapor
was directly measured and controlled by the calibrated mass
flow controller. For gaseous materials, calibration of the mass
flow controllers was made with a gas meter or a soap-film flow
meter. For liquid materials (fluorinated alcohols), calibration
of the mass flow controller was made by measuring the time-
pressure relationship in the vessel with a known volume using
a capacitance manometer, during which the sample vapor was
supplied to the evacuated vessel through the mass flow con-
troller. The total gas pressure of the reactor was monitored by
using a capacitance manometer (MKS Baratron), and was kept
constant by an electrically controlled exhaust throttle valve
located downstream of the reactor. The temperature of the
Figure 3 shows a typical example of a pseudo-first-order OH
decay plot obtained with the DF method for various CF3CH2-
OH concentrations. Since these plots show a linear relationship,
the pseudo-first-order rate constant (kobs) can be derived from
the slopes of the straight lines by least-squares fit to each decay
plot. In Figure 4, the observed pseudo-first-order rate constants
are plotted against CF3CH2OH concentration. In the case of the
DF method, a small correction factor (usually 1 to 3%) is applied
to each pseudo-first-order rate constants to account for the axial
3
diffusion effects. The plotted points are distributed along a
straight line, and the bimolecular rate constant for the reaction
of OH with CF3CH2OH can be derived from the slope by the