Rate Coefficients for Reaction of OH with HFCs
J. Phys. Chem. A, Vol. 110, No. 21, 2006 6725
Therefore, we only briefly describe here the essentials needed
to understand the present investigation.
calibrated electronic mass flow meters. Flow meters were
calibrated independently for each reactant. The reactant con-
centration in the gas flow was also measured by infrared
absorption at 298 K as described below. The reactant concentra-
tion in the reactor was corrected for the differences in temper-
ature and pressure and for dilution. The concentrations of
CF3CH2CH2, CF3CHFCH2F, and CHF2CHFCHF2 in the reactor
were varied in the ranges (2.8-44) × 1014, (2.2-54) × 1014,
and (2.3-66) × 1014 molecule cm-3, respectively. The con-
centration determined using flow rates agreed with that from
infrared absorption measurements to within (5% under all
experimental conditions.
Rate Coefficient Measurements. The rate coefficients k1-
k3 were determined under pseudo-first-order conditions in OH
concentration using pulsed laser photolysis (PLP) production
of OH and its laser-induced fluorescence (LIF) detection. The
LIF reactor consisted of a 15-cm-long jacketed Pyrex cell with
an internal volume of ∼200 cm3. Orthogonal ports on the reactor
were used to propagate the laser beams. The photomultiplier
tube (PMT) detector was mounted on a port orthogonal to the
laser beams. The LIF reactor temperature was regulated to (1
K by circulating heated/cooled silicon oil through its jacket.
The gas mixture entering the reactor attained the temperature
of the reactor before reaching the reaction zone, defined by the
intersection of the photolysis beam and probe laser beam. The
temperature of the gases in the reaction zone was directly
measured with a calibrated thermocouple inserted into the gas
flow. The thermocouple was withdrawn from the detection
region while measuring the OH temporal profiles. Pressures in
the LIF reactor were measured with a 10, 100, or 1000 Torr
capacitance manometer.
Infrared Absorption Cross-Section Measurements. Infra-
red (IR) absorption cross-sections of the HFCs were measured
using a Fourier transform infrared spectrometer (FTIR) equipped
with a 15-cm-long, 2.5-cm-diameter Pyrex absorption cell with
KBr windows. An incandescent light source, KBr beam splitter,
and liquid N2 cooled HgCdTe (MCT) detector were used.
Spectra were recorded at a spectral resolution of 1 cm-1 over
the range 500 to 4000 cm-1 with 100 coadded scans. The IR
cross-sections were measured by filling the absorption cell with
1-3 Torr of the compound measured using a 10 Torr capaci-
tance manometer. A minimum of 6 concentrations were used
for each compound. The peak absorbance for each band varied
linearly with concentration, i.e., obeyed Beer-Lambert’s law.
Peak absorption cross-sections were obtained using linear least-
squares fits of absorbance versus concentration. The absorption
spectra over the entire wavelength region were converted to
cross-sections using the cross-sections derived at the peaks. The
cross-sections derived from different peak cross-sections agreed
within 5%. Spectrum measurements were also made with the
absorption cell pressurized with 100 Torr of N2 to investigate
the broadening of the HFC bands; the bands were not broadened
at this pressure. Therefore, the IR cross-sections obtained using
the samples alone are applicable under atmospheric pressures.
Rate coefficients were measured at total pressures in the range
of 50 to 60 Torr (He) with linear gas flow velocities in the LIF
reactor of 10 to 20 cm s-1. This flow provided a fresh gas
mixture for each photolysis laser pulse (10 Hz).
OH radicals were produced by 248 nm excimer (KrF) laser
photolysis of H2O2
H2O2 + hν f OH + OH
(4)
where the quantum yield for OH production in reaction 4 is 2.
OH radicals were excited in the A2Σ+ r X2Π band (282
nm) using the frequency-doubled output of a pulsed Nd:YAG
pumped dye laser. The laser-induced fluorescence was detected
by a PMT after it passed through a band-pass filter (peak
transmission at 310 nm with a band-pass of (20 nm, fwhm).
The PMT signal was averaged at various reaction times, ranging
from 10 µs to 50 ms, with a gated charge integrator and recorded
for subsequent analysis.
The initial OH radical concentration, [OH]0, was estimated
from the measured laser fluence (varied over the range 1.0-
6.8 mJ cm-2 pulse-1), the absorption cross-section of the
precursor at the photolysis wavelength, its OH quantum yield,
and the precursor concentration. [OH]0 values in the range 1.2
× 1011 to 7.5 × 1011 molecule cm-3 were used over the course
of the kinetic measurements.
Materials. He (99.999%) was used as supplied as the buffer
gas in all the kinetic measurements. Nitrogen (>99.99%) was
used as supplied in the measurement of IR absorption cross-
sections. Concentrated hydrogen peroxide (>95%, by mole
fraction, as determined by titration with a standard solution of
KMnO4) was prepared by bubbling N2 for several days through
a H2O2 sample which was initially ∼60% by mole fraction. A
small flow of He, approximately 1% of the total gas flowing
through the reactor, was passed through a bubbler containing
the >95% pure liquid H2O2. This mixture from the bubbler was
added to the main gas flow before entering the LIF reactor.
During low-temperature kinetic measurements, the H2O2 res-
ervoir was maintained at a temperature lower than that of the
LIF reactor to avoid possible condensation of H2O2 in the cold
reactor. Ozone was prepared by passing O2 through a com-
mercial ozonizer and stored on a silica gel at 195 K. A dilute
mixture of ozone in He was prepared in a darkened Pyrex bulb
from this sample.
The concentration of H2O2 in the LIF reactor was estimated
from the first-order rate coefficient for loss of OH measured in
the absence of the reactant and attributed to the reaction of OH
with H2O2
OH + H2O2 f HO2 + H2O
(5)
where k5(T) ) 2.9 × 10-12 exp(-160/T) cm3 molecule-1 s-1 6
.
Impurities in Excess Reactant. The rate coefficients for
reactions 1-3 are relatively small, <2 × 10-13 cm3 molecule-1
s-1, and hence, reactive impurities can lead to systematic errors
in the measured values. Unsaturated hydrocarbon impurities,
which can react with OH with rate coefficients of up to 3 orders
of magnitude faster than the HFCs, are therefore of concern.
The HFC samples were analyzed by gas chromatography-mass
spectroscopy (GCMS) using a capillary GS-Al column. No
measurable impurities were observed in the CF3CH2CH3 sam-
ple. The CF3CHFCH2F sample was found to have trace
amounts, <100 ppmv, of CF3CHFCHF2, CF3CH2CH2CF3, and
The concentration of H2O2 in the LIF reactor was varied between
1.6 × 1013 and 1.2 × 1014 molecule cm-3 over the course of
the kinetic measurements but was maintained constant during
each individual rate coefficient determination. The ozone
concentration in the LIF reactor, typically 1 × 1012 molecule
cm-3, was determined from measured flow rates and pressures.
The concentrations of the HFC reactants were determined
by two independent methods. It should be noted that the
concentrations of the reactant in the reactor were not directly
measured. The reactant concentration prior to entering the
reactor was determined from the flow rate measured using