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The multiple role of bromide ion in PPCPs degradation under UV/chlorine treatment Shuangshuang Cheng, Xinran Zhang, Xin Yang, Chii Shang, Weihua Song, Jingyun Fang, and Yanheng Pan Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.7b03268 • Publication Date (Web): 16 Jan 2018 Downloaded from http://pubs.acs.org on January 16, 2018
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The multiple role of bromide ion in PPCPs degradation under UV/chlorine treatment
2 3
Shuangshuang Cheng1,#, Xinran Zhang1,#, Xin Yang1,*, Chii Shang2, Weihua Song3, Jingyun
4
Fang1, Yanheng Pan1
5 6 7 8
1
9
of Environmental Pollution Control and Remediation Technology, Sun Yat-sen University,
School of Environmental Science and Engineering, Guangdong Provincial Key Laboratory
10
Guangzhou 510275, China
11
2
12
and Technology, Clear Water Bay, Kowloon, Hong Kong
13
3
14
China
Department of Civil and Environmental Engineering, the Hong Kong University of Science
Department of Environmental Science & Engineering, Fudan University, Shanghai 200433,
15
16
# First author
17
*Corresponding author: Tel:+86-2039332690; Email:
[email protected] (X. Yang)
18 19 20 21 1
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ABSTRACT
23
This study investigated the role of bromide ions in the degradation of nine
24
pharmaceuticals and personal care products (PPCPs) during the UV/chlorine treatment of
25
simulated drinking water containing 2.5 mgC/L natural organic matter (NOM). The kinetics
26
of contributions from UV irradiation and from oxidation by free chlorine, free bromine,
27
hydroxyl radical and reactive halogen species were evaluated. The observed loss rate
28
constants of PPCPs in the presence of 10 µM bromide were 1.6 to 23 times of those observed
29
in the absence of bromide (except for iopromide and ibuprofen). Bromide was shown to play
30
multiple roles in PPCP degradation. It reacts rapidly with free chlorine to produce a trace
31
amount of free bromine, which then contributes to up to 55% of the degradation of some
32
PPCPs during 15 minutes of UV/chlorine treatment. Bromide was also shown to reduce the
33
level of HO• and to change the reactive chlorine species to bromine-containing species, which
34
resulted in decreases in ibuprofen degradation and enhancement in carbamazepine and
35
caffeine degradation, respectively. Reactive halogen species contributed to between 37 and
36
96% of the degradation of the studied PPCPs except ibuprofen in the presence of 10 µM
37
bromide ion. The effect of bromide is non-negligible during the UV/chlorine treatment.
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INTRODUCTION Pharmaceuticals and personal care products (PPCPs) have been detected in water sources
41
1-4
42
around the world
. Drinking water treatment primarily relies on adsorptive and oxidative
43
processes to abate dissolved contaminants. Studies have indicated that coagulation,
44
sedimentation, and filtration achieve only minimal removal of PPCPs 5. Free chlorine only
45
selectively reacts with PPCPs bearing phenolic, aniline or amine groups 6. Ultraviolet (UV)
46
light at 254nm photodegrades some PPCPs, but works poorly with UV-resistant PPCPs such
47
as carbamazepine at common disinfection doses (up to 500 mJ cm-2) 7, 8.
48
Advanced oxidation processes (AOPs) are potentially attractive alternatives for removing
49
PPCPs from drinking water 9. Recently the combination of UV irradiation and chlorination
50
(UV/chlorine), one type of AOP, obtained great attention due to the fact that UV/chlorine has
51
exhibited better efficiency in degrading PPCPs than either UV irradiation or chlorination
52
alone
53
upstream of a UV contactor with chlorine contact time varying from seconds to minutes. UV
54
irradiation of free chlorine (HOCl/OCl-) produces highly reactive hydroxyl radicals (HO•) and
55
chlorine radicals (Cl•) 12. Cl• reacts with chloride ion to form dichlorine radicals (Cl2•-) and the
56
reactions of HO• and Cl• with HOCl/OCl- produce oxychlorine radicals (ClO•)
57
presence of HO• and Cl• during UV/chlorine treatment has been directly proved by using
58
electron spin resonance
59
exploring the degradation of reference compounds-benzoic acid and 1,4-dimethoxybenzene
60
14, 15
61
halogen species (RHS, here refers to radicals only) can all degrade PPCPs, but UV irradiation
10, 11
. UV/chlorine application in drinking water can be operated by adding chlorine
13
12
. The
and the existence of Cl2•- and ClO• was indirectly evidenced by
. During the UV/chlorine process, UV irradiation, HOCl/OCl- oxidation, HO• and reactive
3
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generally has not contributed significantly to PPCP reduction 8. For chlorine-resistant
63
compounds such as carbamazepine, caffeine, atrazine, DEET, and ibuprofen, HO• and RHS
64
play the dominant roles in their degradation
65
react with electron-rich moieties. The reactivity of RHS with aromatic PPCPs depends on the
66
electron-donating properties of substituents on aromatic ring
67
chlorine adduct formation are reported to be the major mechanisms for chlorine radical
68
reactions
69
aromatic ring) and it can also react with unsaturated compounds to produce Cl adducts (∼106
70
-108 M-1s-1 for double bonds)
71
HO• to yield a hydroxycyclohexadienyl radical with the reaction rate about 1010 M-1s-1 19, 21.
72
Reaction of ClO• with organic compounds is about two or three orders of magnitude slower
73
than that for Cl• 19.
74
16-18
. RHS has been reported to preferentially
15
. Hydrogen abstraction and
19
. Cl2•- can abstract hydrogen slowly from organic compounds (≤107 M-1s-1 on
20
. The addition of Cl• to the benzene ring is similar as that of
In natural waters, bromide is present at concentrations ranging up to tens of µM
22
.
75
The presence of bromide may affect the rate of degradation of PPCPs during UV/chlorine
76
treatment, but this has not been previously investigated. The reaction of bromide with
77
HOCl/OCl- produces free bromine (HOBr/OBr-) (Eq. 1). HOBr is highly reactive towards
78
phenolics and amines
79
phenols
80
17α-ethinylestradiol and benzophenone-3, is considerably faster at bromide concentrations of
81
tens of µgL-1 during chlorination in the dark
82
HO• and Br• and oxybromine radicals (BrO•) can also form (Eq. 2 and 3).
83
than
HOCl
23
, which is about three orders of magnitude more reactive toward 24
.
The
transformation
of
phenolic
compounds,
19, 25-27
including
. The UV irradiation of HOBr generates
HOCl + Br − → HOBr + Cl −
1.6× 103 M-1s-1 4
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hv HOBr → HO• + Br •
85
HOBr + HO • → BrO • + H 2O
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(2) 2.0× 109 M-1s-1
(3)
86
Bromide ion is also known to be a HO• scavenger, forming radicals such as BrOH•-, Br•
87
and Br2•- (Eq. 4–7) 28. Meanwhile, bromide also reacts with Cl• and Cl2•- to form ClBr•- (Eq. 8
88
and 9) 29. •
OH + Br − → BrOH • −
1.1× 1010 M-1s-1
(4)
90
BrOH •− + H + → Br • + H 2O
4.4× 1010 M-1s-1
(5)
91
Br • + Br − → Br2
1.2× 1010 M-1s-1
(6)
92
BrOH •− + Br − → Br2•− + OH − 1.9× 108 M-1s-1
(7)
93
Cl • + Br − → BrCl •−
1.2× 1010 M-1s-1
(8)
94
Cl2•− + Br − → BrCl •− + Cl −
4.0× 109 M-1s-1
(9)
89
•−
95
It should be noted that the bromine radicals including BrOH•-, Br•, Br2•- and BrO• have not
96
been directly analyzed by electron spin resonance during UV/chlorine treatment of
97
bromide-containing waters. They are proposed to be present based on the advanced oxidation
98
chemistry involving bromide, which has been extensively studied
99
the mixture of chlorine and bromine radicals in the system, there are no available methods to
100
directly or indirectly obtain their levels currently. Models thus are developed to reflect their
101
steady-state concentrations under varying reaction conditions and they have been used to
102
evaluate UV/hydrogen peroxide, UV/peroxodisulfate and UV/chlorine AOP processes 14, 17, 28,
103
32-34
104
be expected to affect PPCP degradation in the UV/chlorine process. The presence of bromide
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can either enhance or diminish PPCP degradation and the potential enhancement is a function
28, 30, 31
. Meanwhile, due to
. The above reactions involving bromide can alter the speciation of RHS and would thus
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of the complex chemistry of the radicals. Increasing bromide concentration has been reported
107
to decrease the degradation rate of phenol during UV/H2O2 treatment. Grebel et al reports that
108
Br2•- accounted for 24% of the phenol destruction while HO• accounted for 75% from model
109
prediction
110
presence of both chloride and bromide due to the dominant formation of ClBr•-, which is
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highly reactive toward electron-rich moieties 32. Caffeine has been reported to degrade faster
112
in seawater containing both bromide (0.85 mM) and chloride (420 mM) than in fresh water
113
under UV/chlorine treatment
114
directly relevant to UV/chlorine drinking water treatment, but they suggest that bromide must
115
be expected to have great impact on PPCPs degradation during UV/chlorine treatment of
116
drinking water.
33
. The UV/H2O2 degradation of acetaminophen was greatly enhanced in the
17
. Those limited data were obtained under conditions not
117
This study was designed to examine the impact of bromide ions during the UV/chlorine
118
treatment and gain insight into the role of bromide ions in PPCP degradation in this process.
119
The degradation kinetics with and without bromide were evaluated. The contributions to
120
PPCP degradation from UV irradiation and from oxidation by free chlorine (78% HOCl/ 22%
121
OCl- at pH 7.0), free bromine (mainly HOBr at pH 7.0, ∼97%), HO• and RHS were quantified
122
to assess the importance of these reactions and to discover the inherent bromide effects. Nine
123
PPCPs frequently detected in the aqueous environment were tested at a concentration of 500
124
ngL-1 in a 2.5 mgCL-1 natural organic matter (NOM) solution to simulate the feed water in
125
drinking water purification. Two bromide concentrations were tested: 80 µgL-1 (1 µM) and
126
800 µgL-1 (10 µM).
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MATERIALS AND METHODS
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Chemicals. The nine PPCPs tested were caffeine (CAF), iopromide (IPM), bisphenol-A
130
(BPA), diclofenac (DCF), triclosan (TCS), acetaminophen (ACE), carbamazepine (CBZ),
131
sulfamethoxazole (SMX) and ibuprofen (IBU). All were purchased from Sigma-Aldrich
132
(USA). Their structures and their chemical properties are listed in Table 1. The molar
133
concentrations of the spiked PPCPs are shown in Table S1. An NOM stock solution was
134
prepared by dissolving Suwannee River NOM isolate (Cat. No. 2R101N, International Humic
135
Substances Society) into ultrapure water and filtered by 0.45 µm glass fiber membrane
136
pre-ashed at 500oC. The other chemicals and reagents used are described in the Supporting
137
Information (Text S1).
138
UV/chlorine experiments. Monochromatic UV irradiation at 253.7 nm was applied
139
through an apparatus containing three 10W low-pressure mercury lamps which delivered a
140
quasi-collimated beam. The photo fluence rate at 254 nm received in the reactor was
141
2.24×10-7 E·L-1·s-1 determined according to iodide-iodate chemical actinometry, and the
142
corresponding average UV254 fluence rate was 0.55 mW/cm2
143
diameter was placed directly under the beam.
35
. A cylindrical dish 7 cm in
144
The NOM stock solution was diluted to 2.5 mgL-1 as DOC before each experiment. The
145
stock solutions of the PPCPs were spiked to achieve a concentration of 500 ngL-1 of each
146
tested PPCP (6.32×10-4 µM to 3.31×10-3 µM in molar concentration, Table S1). Bromide was
147
added to some of the samples to achieve a concentration of 1 or 10 µM, as required. All of the
148
samples were buffered to pH 7.0 with 10 mM phosphate buffer. In the UV/chlorine treatment,
149
the chlorine concentration was 70 µM and the accompanied chloride ion addition was 84.5 7
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µM. The concentration of chloride ion in NaOCl solution was 84.5 µM. It was determined by
151
subtracting free chlorine concentration from analyzed chloride concentrations in Na2S2O3
152
quenched NaOCl solution. The solution containing NOM, PPCPs and bromide was mixed
153
first. When exposed to the UV light, chlorine was added immediately to the mixing solution
154
and was set as the beginning of the UV/chlorine experiment. UV irradiation alone without
155
free chlorine addition was also tested, as was chlorination at 70 µM in the dark. At different
156
time intervals (0.5-15 min), samples of the mixture being treated were quenched with sodium
157
thiosulfate, followed by solid phase extraction (SPE) for PPCP analysis. The 15-min
158
irradiation corresponded to a fluence of 495 mJ/cm2. The chlorine residuals were recorded in
159
separate tests following these same procedures. In the absence of bromide, the chlorine
160
residuals were analyzed using the DPD ferrous titration method. In the presence of bromide,
161
that same method was used to quantify the total residuals. Bromine residuals were determined
162
by the spectrophotometric phenol red method measuring the absorbance at 592 nm 36. The
163
details are provided in Text S2 in the Supporting Information. Thus, the concentration of free
164
chlorine was obtained by subtracting the bromine concentration from the total residual
165
concentration. The control experiments in the dark were also conducted by dosing 5 mgL-1
166
free chlorine (HOCl/OCl-) or 1 mgL-1 free bromine (HOBr/OBr-) to the NOM solution (2.5
167
mgL-1 as DOC) containing 500 ngL-1 of each PPCP at pH 7.0. The residual free chlorine and
168
bromine concentrations were recorded at different reaction intervals. In order to find the
169
halogenated products, bromide (0, 5, 50, 100 µM), PPCPs (1 mgL-1) and free chlorine (280
170
µM) were spiked or dosed at pH 7.0 at high concentrations compared to the PPCP degradation
171
tests. 8
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Determining the rate constants for the PPCPs’ reactions with HOBr. HOBr stock
173
solution was produced by mixing NaOCl with a slight stoichiometric excess of bromide (5%)
174
37
175
at room temperature (23±2°C). The experimental details are provided in Text S3, Table S2
176
and Figure S1 in the Supporting Information.
. The kinetic tests were conducted in the presence of 10 mM phosphate buffer at pH 7.0 and
177
Determining the steady state HO• concentrations. HO• concentrations were inferred
178
indirectly by measuring the depletion of a HO• probe, nitrobenzene (NB). NB (50 nM) was
179
added to the solutions before UV/chlorine treatment. The decay of NB over time was
180
analyzed by HPLC at 265 nm (Dionex U3000). The steady state HO• concentrations were
181
calculated by using Eq. 10.
182
−
d [ NB] = (k HO •, NB [ HO • ]ss + kUV + kvol )[ NB ] = k obs , NB [ NB ] dt
(10)
183
where kHO•,NB is the reaction rate constant between NB and HO•, taken as 3.9 × 109 M-1s-1 14 .
184
kUV and kvol represent the observed first-order rate constants of NB’s disappearance through
185
direct UV photolysis and volatilization, respectively. The details of the tests are presented in
186
Text S4 in the Supporting Information.
187
Modeling of the RHS’ kinetics. Version 5.55 of the Kintecus software was used to
188
model the radical concentration data (Table S4), as the steady-state concentrations of the RHS
189
could not be determined experimentally. Several studies have successfully applied this model
190
to predict the fates of hydroxyl and halogen radicals, confirming good agreements between
191
the modeled results and experimental results
192
constant for the reactions between the RHS and the PPCPs and NOM, the kinetic modeling
193
only considered the reactions involving inorganic components without the incorporation of
32-34, 38, 39
. Because there was no available rate
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PPCPs and NOM to evaluate the concentrations of inorganic radicals in the initial 5 minutes
195
after the initiation of the reactions. The 5-min scale enables achieving pseudo-steady-state
196
concentrations. It should be noted that many radicals such as BrOH•-, Br•, Br2•- and BrO•
197
haven’t been directly proved during UV/chlorine process. The kinetics model just simply
198
hypothesized based on reactions reported in the literature and the known chemistry of the
199
system
200
radical reactions, but rather as an aid to highlight probable radical reactions. In this study, as
201
NOM, PPCPs and their products may partially scavenge the radicals, this model was merely
202
applied to indirectly reflect the concentrations variance of hydroxyl and reactive halogen
203
radicals in pure solution with/without bromide ions added.
33, 34
-
and the model used here was not intended to provide a means of confirming
204
Calculating the contributions from UV, free chlorine (HOCl/OCl-), free bromine
205
(HOBr/OBr-), HO• and RHS. The degradation of PPCPs during UV/chlorine treatment can
206
involve contributions from UV direct photolysis, oxidation by free chlorine (HOCl/OCl-), HO•
207
and RHS, and free bromine (HOBr/OBr-) oxidation when bromide is present. The degradation
208
of a specific PPCP (expressed as S) can be thus written as in Eq. 11.
209
−
d[S ] = k 'UV [S] + k free chlorine[free chlorine][S] + k free bromine[free bromine][S] + k HO• [HO• ][S] + k RHS[RHS][S] dt (11)
210 211
Where [S] is the concentration of a specific PPCPs; kUV′ is the pseudo–first-order decay
212
rate constant of a PPCP by UV photolysis; kfree chlorine, kfree bromine, kHO•,and kRHS represent the
213
apparent second-order rate constants specific to pH 7 between the PPCP and free chlorine,
214
free bromine, HO• and RHS present, respectively.
215
The remaining concentration of a PPCP ([S]t) at a specific reaction time then can be 10
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calculated by numerical (stepwise) analysis using Eq. 12. t
t
t
0
0
0
[S]t − [S]0 = − ∫ k 'UV [S]dt − ∫ k free chlorine[free chlorine][S]dt − ∫ k free bromine[free bromine][S]dt t
t
0
0
(12)
− ∫ k HO• [HO• ][S]dt - ∫ k 'RHS[RHS][S]dt 218 219
The removal attributable to each process was calculated separately in Text S5. The fractional removals (R) can thus be expressed as in Eq. 13: t
[S] − [S]t R= 0 = [S]0
∫k 0
' UV
[S]dt
[S]0 t
220
∫k + 0
HO•
t
∫k + 0
[free chlorine][S]dt
free chlorine
[S]0
[HO• ][S]dt [S]0
t
∫k + 0
t
∫k + 0
' RHS
[RHS][S]dt [S]0
[free bromine][S]dt
free bromine
[S]0
(13)
= RUV + R free chlorine + R free bro min e + RHO• + RRHS 221
The contribution percentages attributable from each species hereafter refers to the percentages
222
calculated based on the original concentrations of PPCPs, not the overall removal of PPCPs.
223
Analytical methods. DOC concentrations were measured using a Shimadzu
224
TOC-VCPH analyzer. The SPE procedures followed a revised method proposed by
225
Yang’s group 40 and the details are provided in Text S6 in the Supporting Information.
226
Products analysis is provided in Text S7.
227 228
RESULTS AND DISCUSSION
229
PPCP oxidation kinetics during UV/chlorine treatment. The observed first-order loss
230
rate constants of PPCPs in the absence and presence of 1 and 10 µM bromide at pH 7.0 are
231
shown in Figure 1. The observed loss rate constants in the presence of 1 µM bromide
232
increased by 12 to 210% for majority of the PPCPs except IBU compared to the absence of
233
bromide. This enhancement was enlarged when the bromide concentration increased with
234
exception of IPM and IBU. In the absence of bromide, observed pseudo-first order rate 11
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coefficients for the PPCPs ranged from 6.1 × 10−4 to 6.6 × 10−2 s−1. IBU, CBZ and CAF had
236
the slowest decay rate constants, which were 5.4 × 10−4, 6.1 × 10−4 and 6.6 × 10−4 s−1,
237
respectively, indicating that they were more resistant compared to other PPCPs. SMX was
238
removed quickly with an observed loss rate constant of 6.6 × 10−2 s−1. SMX features a primary
239
amine that reacts quickly with free chlorine (940 M-1s-1) 6. The other PPCPs, containing either
240
secondary amine (DCF) or a phenolic group (TCS, ACE, BPA), had modest removal rate
241
constants in the range of 10−3 to 10−2 s−1. IPM has iodine and amide groups in its molecule.
242
Iodine can be substituted by a hydroxyl group toward the reaction with HO• 41, 42.
243
In the presence of 10 µM bromide, most of the PPCPs still followed first-order decay
244
kinetics except that CAF, CBZ and IBU had a relatively low correlation coefficient R2
245
(0.88104 M-1s-1).
413
Group II PPCPs have modest to fast overall degradation rates and are primarily degraded
414
by RHS and/or HO• oxidation. They react slowly or not at all with HOCl/OCl- (< 1 M-1s-1)
415
and HOBr. The PPCPs in this group may contain electron rich moieties, but generally weaker
416
electron-donating moieties compared to amine and phenolic moieties. IPM, CAF and CBZ are
417
in Group II.
418
Group III PPCPs have low to modest degradation rates, but they are primary degraded by
419
HO• oxidation. PPCPs in this group do not contain electron-rich moieties. The representative
420
in this study was IBU.
421
Figure 4 illustrates the reaction pathways involved in UV/chlorine treatment when
422
bromide ion is present. The bromide affects the three groups of PPCPs through different
423
reaction mechanisms. Indeed, bromide plays multiple roles. On the one hand, it rapidly reacts
424
with HOCl to produce HOBr. HOBr’s reaction rate constants with primary and secondary
425
amines and phenolic compounds are around one to three orders of magnitude higher than
426
those of HOCl, so a trace amount of bromide in the solution will promote Group I PPCP
427
degradation. On the other hand, bromine radicals form from free bromine photolysis and from
428
bromide’s reaction with HO• and chlorine radicals. The presence of bromide then reduced the
429
levels of HO• and changes the RHS speciation-reducing reactive chlorine species and
430
forming reactive bromine species. The reactive bromine radicals react with electron-rich
431
moieties more selectively than chlorine radicals 45,51, significantly affecting the degradation of
432
Group II PPCPs. Some PPCPs, such as CBZ and CAF, benefit from the presence of reactive 20
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433
bromine radicals (e.g. ClBr•- and BrO•). On the contrary, the degradation of some PPCPs, like
434
IPM, was retarded due to the decrease in reactive chlorine radcials. For Group III PPCPs like
435
IBU, the presence of bromide decreased the overall degradation rate due to the decrease in
436
HO• levels.
437
As a result of bromide-involved reactions, brominated transformation products from degradation
were
identified
(Table
S6).
At
a
low
dose
ones
and
438
PPCP
439
of bromide (5 µM), chlorinated products were the
440
brominated products generally contained one bromine atom in their molecules. With
441
increasing bromide concentrations, shifting from chlorinated to brominated products
442
was clearly shown. At a high dose of bromide (50 and 100 µM), brominated products
443
become the dominated ones and the brominated products generally contained one or
444
two bromine atoms. In some products, both chlorine and bromine atoms were present.
445
It should be noted that more chlorinated and brominated products were observed in the
446
presence of UV light (Table S6) than in the absence of UV light (Table S7), which
447
were due to the halogenation reactions from RHS in addition to HOCl/OCl- and
448
HOBr/OBr-. We did not intend to identify of the structures of the transformation
449
products in this study, but further research is needed to improve understanding the
450
formation mechanisms of the brominated products and their associated toxicity.
predominant
451
Environmental implications. Bromide ion is present in water sources at concentrations
452
ranging from ∼10 to >1000 µgL-1 22. It potentially impacts the chemical oxidation treatment of
453
water supplies due to the formation of free bromine and/or reactive bromine radicals. The
454
multiple role of bromide in micropollutant abatement under the UV/chlorine process has been 21
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demonstrated in this study. Under the UV/chlorine treatment, despite the quenching effect on
456
HO• by bromide and resulting decreases in HO•-driven removal of PPCPs (Group III), faster
457
degradation of many PPCPs (Group I and II) may occur in bromide-rich waters due to free
458
bromine and RHS-mediated reactions. It should be noted that the increase is already
459
significant at 1 µM bromide level. Thus, the bromide effects are expected to be observable for
460
waters with bromide concentrations at sub micromolar or higher levels. This study classified
461
PPCPs into three groups based on their reactive moieties and the contribution of reactive
462
oxidant species. The principles obtained can be applied to predict the degradation
463
performance of other PPCPs in bromide-containing waters under UV/chlorine treatment. This
464
study provides new insights on such reactions and improves the understanding of
465
micropollutant degradation in the UV/chlorine treatment.
466
Although the scope of this study focused on the drinking water treatment, UV/chlorine
467
processes could also be applied for wastewater reclamation or industrial wastewater, where
468
higher amount of bromide will impact the removal efficiency of micropollutants. Future
469
efforts should consider the bromide effects in complicated water matrices and the role of
470
water constituents, such as alkalinity and ammonium N. For example, carbonate can scavenge
471
HO•, Cl•, Cl2•- and BrCl• to form carbonate radicals, which will change the levels and the
472
distribution of the radicals in the UV/chlorine process. The individual contributions from
473
different RHS should also be investigated. Moreover, the transformation byproducts
474
containing bromine can form from the reaction with free bromine and RHS under
475
UV/chlorine conditions in presence of bromide and need further evaluation. Work is on-going
476
in our laboratory to evaluate the yields and risks associated with the formation of these 22
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Page 24 of 39
byproducts.
478 479
Acknowledgements We thank the National Science Foundation of China (grants 21577178 and 21622706),
480 481
Guangdong’s
Natural
Science
Funds
for
Distinguished
Young
Scholars
(grant
482
2015A030306017), and the Fundamental Research Funds for the Central Universities (grant
483
17lgjc16 and 17lgpy93) for their financial support of this study.
484 485
Supporting information Details of analytical methods and additional figures are included. This material is
486 487
available free of charge via the Internet at http://pubs.acs.org.
488
Information on PPCP and transformation products analysis, bromine reaction rate
489
constants, Kintecus model for radical concentration prediction and etc. (Text S1-S7, Table
490
S1-S6, and Figure S1-S6).
491 492
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Table 1. Information on the PPCPs tested.
PPCP
Bisphenol-A (BPA)
pKa
kHO· (109 M-1s-1)
kapp, chlorine pH=7 (M-1s-1)
kapp,bromine pH=7 (M-1s-1) (this study)
9.6, 10.2
6.9 52
62 23
9.4×104
7.9
9.7 53
4.7×102 54
8.6×104
13 56
2.6×104
9.4×102 6
3.0×104
Structure
HO
OH
Cl
OH
Triclosan (TCS)
O
Cl
Cl
H N
Acetaminophen (ACE)
2.2 55
9.71 O
HO
Sulfamethoxazole (SMX)
O NH2
S
O
N
NH
1.69, 5.57
O
5.5±0.7 57
O
Diclofenac (DCF)
Cl
3.89±1.17
OH H N
58
3.8×104
5.9 59