saturated stock solutions were prepared under nitrogen. Fresh
stock solutions of CHBr3 were made daily because of its slow
hydrolytic decomposition. The pH of the suspension was
adjusted with 1 N HClO4 or 1 N NaOH and was measured
before and after the irradiation. CCl4 (Baker), CHCl3 (Baker),
CCl3COONa (Aldrich), and CHBr3 (Aldrich) were used as
received.
phase were sampled, filtered, and injected into the same glass
vial descibed above. In order to drive aqueous carbonate
species into the gas phase (for CO2 analysis), 100 µL of
concentrated sulfuric acid was added. The vial was then
shaken and left for at least 30 min for equilibration before GC
analysis. Standard solutions of sodium carbonate for CO2
analysis were prepared by the same method.
Irradiations were performed with a 1000-W Xe arc lamp
(Spindler and Hoyer) operated at 910 W. Light was filtered
through a 10-cm IR water filter and, when light intensities
needed to be measured, a UV band pass filter (310-400 nm,
Corning). The filtered light was focused through a convex
lens onto a reactor cell loaded with the TiO2 suspension. Light
intensity measurements were performed by chemical acti-
nometry using (E)-R-(2,5-dimethyl-3-furylethylidene) (iso-
propylidene) succinic anhydride (Aberchrome 540) (16). A
typical light intensity through a UV band pass filter was ∼1.4
The Cl- production after the photolysis was measured
with an Orion chloride ion-selective electrode (Model 96-
17B). Gaseous samples from the gas collecting tube and the
head space of the glass vials were analyzed by a GC (Carle
AGC series 400) equipped with a thermal conductivity detector
and columns of Porapak QS and 5-Å molecular sieve particles.
Helium was used as the carrier gas. Duplicate measurements
were made for each sample with an injection volume of 20
µL. Standards of gaseous CO and CO2 were made by mixing
each gas with He at known ratios in the gas collecting tube.
The total numbers of CO and CO2 molecules generated during
the photolysis were calculated by using Henry’s law constants
based on the assumption of liquid-gas equilibrium.
× 10-3 Einstein L-1 min-1
.
Two distinct types of photolysis experiments were carried
out. One set of experiments was focused on the formation
of halogenated intermediates and halide ions and the
disappearance of substrate compounds as a function of
irradiation time; another set was focused on the determination
of gaseous CO and CO2 generation after 2 h of irradiation.
The two sets of photolysis experiments were performed in
different reactors as described below.
Photolysis and Analysis of Halogenated Com pounds and
Halide Ions. For the experiments in which halogenated
intermediates and halide ions were determined, a 35-mL
quartz reactor cell was used. After gas saturation, reagents
(an aliquot of the saturated stock solution and alcohols as an
electron donor for CCl4 degradation) were added into the
reactor with minimal head space through a rubber septum.
Light was irradiated through a UV band pass filter.
Sample aliquots were obtained with a 1-mL syringe, filtered
through a 0.45-µm nylon filter, and injected into a 2.5-mL
glass vial having a screwtop cap and a Teflon-faced septum.
Halogenated compounds and their degradation intermediates
were extracted with 0.5 mL of pentane immediately after
sampling. Sample vials were stored at 4 °C in the dark up to
48 h before analysis. The degradation and formation of
halogenated compounds and intermediates were followed
chromatographically with a Hewlett-Packard (HP) 5880A gas
chromatograph (GC) equipped with a 63Ni electron capture
detector and a HP-5 column (crosslinked 50% PhMe silicone,
25m × 0.32 mm × 1.05 µm). Nitrogen was used as the carrier
gas. The GCs were calibrated daily with external standards
(CCl4, CHCl3, CHBr3, C2Cl4, and C2Cl6) and duplicate mea-
surements were made for each sample. The formation of
perbromoethylene (C2Br4), whose authentic standard was not
available, was identified with a GC (HP 5890 II) connected to
a mass selective detector (HP 5972A). The aqueous phase in
the sampling vial was analyzed by ion-exchange chroma-
tography (IC) for halide ions. The IC system was a Dionex
Bio-LC system equipped with a conductivity detector and a
Dionex OmniPac PAX-500 column (8 µm × 5 mm × 250 mm).
Photolysis and Analysis of Gaseous Products. The
experiments determining CO and CO2 used a Pyrex reactor
with a total volume of 100 mL. The Pyrex reactor was
connected to a gas collection tube (total volume 145 mL, Ace
Glass) through a glass joint, which was evacuated with a closed
stopcock. After N2 or O2 purging, 0.5 mL of CHCl3 or CCl4 was
added directly into the suspension. By the end of photolysis,
most of CHCl3 dissolved into the aqueous suspension while
excess CCl4 droplets remained at the bottom of the reactor.
A He-filled balloon was then attached to a top opening of the
reactor in order to collect gaeous product evolved during the
photolysis. The full band irradiation (with no filter) lasted
for 2 h. At the end of each photolysis, the evacuated gas
collection tube was filled with the gas mixture in the balloon
and taken for GC analysis. Two aliquots of 1-mL aqueous
Results
Results of the photocatalytic degradations of CHCl3 and CHBr3
under N2 saturation are shown in Figure 1. Even though
dioxygen was considered to be essential for the degradation
of these compounds (5 ,6, 17, 18), they were decomposed
slowly in the N2-saturated photocatalytic systems. The
linearity of halide production over the whole irradiation period
indicates that the contribution from the residual oxygen,
which remains even after vigorous N2 purging, to total halide
production is insignificant. In particular, the degradation
rates were greatly enhanced at pH 12 for both CHCl3 and
CHBr3. Although CHCl3 and CHBr3 can be degraded through
base-catalyzed hydrolysis (eqs 8-10) in the absence of light
(19, 20), the hydrolysis rate at pH 12 is small compared to the
net photolysis rate as shown in Figure 1.
CHX3 + OH- f CX3- + H2O (X ) Cl- or Br-) (8)
CX3- T :CX2 + X-
(9)
:CX2 + H2O f CO + 2H+ + 2X-
(10)
The measured quantum yields for the halide production were
ΦCHCl ) 0.021 (CHCl3 at pH 12), ΦCHCl ) 0.0034 (CHCl3 at pH
3
3
5), ΦCHBr ) 0.018 (CHBr3 at pH 12), and ΦCHBr ) 0.0019 (CHBr3
3
3
at pH 5).
The effects of the dissolved oxygen concentration on the
photolysis rate of CHCl3 are shown in Figure 2. These results
show that O2 increases the net dechlorination rate. The
stoichiometry for the complete mineralization of CHCl3 to
CO2 in the presence of oxygen is (5, 17)
CHCl3 + H2O + 1/ 2O2 f CO2(g) + 3HCl(aq)
∆H298 ) -113.1 kcal/ mol (11)
For CHCl3 photodegradation in an air-saturated solution
(Figure 2a), the Cl- production, however, went beyond the
level of concentration that corresponded to the stoichiometric
consumption of dissolved O2. This result is not consistent
with the observations of Kormann et al. (5). They observed
that [Cl-] increased linearly up to ∼1.4 mM, at which point
the chloride production rate abruptly decreased to a much
smaller value as the O2 was depleted.
The normal effect of [O2] on the dechlorination rate (Figure
2b) exhibited Langmurian dependence (21, 22) except that
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9 0 ENVIRONMENTAL SCIENCE & TECHNOLOGY / VOL. 31, NO. 1, 1997