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Remediation and Control Technologies 3-
Effects of HCO on Degradation of Toxic Contaminants of Emerging Concern by UV/NO
3-
Ying Huang, Minghao Kong, Danielle Westerman, Elvis Genbo Xu, Scott Coffin, Kristin H. Cochran, Yiqing Liu, Susan D. Richardson, Daniel Schlenk, and Dionysios D. Dionysiou Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.8b04383 • Publication Date (Web): 04 Oct 2018 Downloaded from http://pubs.acs.org on October 5, 2018
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Environmental Science & Technology
Effects of HCO3− on Degradation of Toxic Contaminants of
1
Emerging Concern by UV/NO3−
2 3
Ying Huang1, Minghao Kong1, Danielle Westerman2, Elvis Genbo Xu3, Scott Coffin3,
4
Kristin H. Cochran2, Yiqing Liu1,4, Susan D. Richardson2, Daniel Schlenk3, and Dionysios D.
5
Dionysiou1*
6
1Environmental
7
Engineering, University of Cincinnati, Cincinnati, Ohio 45221, USA
8
2Department
9
Carolina 29208, USA
Engineering and Science, Department of Chemical and Environmental
of Chemistry and Biochemistry, University of South Carolina, Columbia, South
10
3Department
11
USA
12
4Faculty
13
Chengdu 611756, China
of Environmental Sciences, University of California, Riverside, California 92521,
of Geosciences and Environmental Engineering, Southwest Jiaotong University,
14 15 16 17
*Correspondence to: Dionysios D. Dionysiou (
[email protected])
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Abstract
20
This study investigated the significant influence of HCO3− on the degradation of
21
contaminants of emerging concern (CECs) during nitrate photolysis at 254 nm for water reuse
22
applications. The second-order rate constants for the reactions between selected contaminants with
23
carbonate radical (CO3•−) were determined at pH = 8.8 and T = 20 °C: estrone ((5.3 ± 1.1) × 108
24
M−1 s−1), bisphenol A ((2.8 ± 0.2) × 108 M−1 s−1), 17α-ethynylestradiol ((1.6 ± 0.3) × 108 M−1 s−1),
25
triclosan ((4.2 ± 1.4) × 107 M−1 s−1), diclofenac ((2.7 ± 0.7) × 107 M−1 s−1), atrazine ((5.7 ± 0.1) ×
26
106 M−1 s−1), carbamazepine ((4.2 ± 0.01) × 106 M−1 s−1), and ibuprofen ((1.2 ± 1.1) × 106 M−1 s−1).
27
Contributions from UV, reactive nitrogen species (RNS), hydroxyl radical (•OH), and CO3•− to the
28
CEC decomposition in UV/NO3− in the presence and absence of HCO3− were investigated. In
29
addition, possible transformation products and degradation pathways of triclosan, diclofenac,
30
bisphenol A, and estrone in UV/NO3−/HCO3− were proposed based on the mass (MS) and MS2
31
spectra. Significant reduction in the cytotoxicity of bisphenol A was observed after the treatment
32
with UV/NO3−/HCO3−.
33
34
Keywords
35
Carbonate radical, UV/NO3−, Contaminants of emerging concern, Cytotoxicity, Water reuse
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Environmental Science & Technology
TOC art ONOO h
CO2
NO3
h
h O2
+ NO2
NO
+O
2
h
37
NO2
h
or +
3
/O
+ NO + OH
H
NO2
OH +HCO3
H
/O
+O
H
OH
h +C O
ONOO
h
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Introduction
39
Nitrate (NO3−) photolysis causes the formation of reactive oxygen species (ROS) and
40
nitrogen species (RNS), nitrite (NO2−) and peroxynitrite (ONOO−), which may pose a health threat
41
in water undergoing treatment1, 2. Irradiation of water containing NO3− under low-pressure (LP)-
42
UV at 254 nm (UV/NO3−) primarily leads to the formation of ONOO−, nitrogen dioxide radical
43
(•NO2), and hydroxyl radical (•OH)3-6. Nitrite formation is mainly ascribed to the decomposition
44
of peroxynitrite when the irradiation wavelength is lower than 280 nm2, 4. Nitrogen oxide radical
45
(•NO) is subsequently produced via the photolysis of nitrate, nitrite, peroxynitrite, and the
46
substantial oxidation of peroxynitrite by •OH7-9. Nitrate photolysis is highly dependent on the
47
reaction pH and the irradiation wavelength6. The primary reactions of nitrate photolysis at 254 nm
48
and high pH (7 ≤ pH < 9) in solutions containing dissolved O2 are summarized in Figure 1.
49
Carbonate radical (CO3•−) can also be formed with low yield during the NO3− photolysis in surface
50
water due to the presence of CO2 via the decomposition of an adduct ONOOC(O)O− produced2.
51
As prevalent anions in natural waters, HCO3−/CO32− play a significant role in NO3− photolysis,
52
affecting the RNS speciation via enhancing the ONOOC(O)O− formation and quenching •OH with
53
the generation of CO3•− (eqs. 1-2)5, 6, 10, 11.
54
•
OH + HCO3― → CO•3 ― + H2O
k = 8.5 × 106 M ―1s ―1
(1)
55
•
OH + CO23 ― → CO•3 ― + OH ―
k = 3.9 × 108 M ―1s ―1
(2)
56
Among the reactive species in UV/NO3− in the presence of HCO3− (UV/NO3−/HCO3−), •OH
57
(E0 = 2.0 V12) is a non-selective oxidant, which could react with various contaminants at high rate
58
constants (> 109 M−1 s−1) through electron transfer, H-abstraction, and radical addition13. These
59
three routes are favorable for •NO2 (E0 = 1.03 V) as well, but it selectively oxidizes anilines,
60
phenolic moieties, phenothiazines, thiols, and ascorbate at lower rate constants12. •NO2-addition
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was observed on the ortho or para-position of -OH group on the aromatic ring due to the
62
electrophilic character2,
63
derivatives stimulate high environmental concern11. Nucleophilic addition on the carbonyl
64
moieties is a well-established pathway for ONOO− (E0 = 1.03 V)2, and it could selectively react
65
with phenolic moieties at relatively high rates14. ROS other than •OH, such as O2•− (consumed
66
rapidly by •NO2 and •NO), O•− (pKa = 11.9), and O(3P) (Φ > 0.1%), are not considered in this study
67
due to their low concentration and weak oxidation ability at high pH under UV254nm 4, 6. The RNS
68
and •OH produced can be utilized to decompose CECs from wastewater during the UV irradiation
69
in the presence of NO3− 11, 15-16. Nevertheless, studies about the effects of HCO3− on various CEC
70
degradation in LP-UV/NO3−, and the resulting environmental impacts of treated solutions are
71
limited11, 16, 17.
11.
The toxicity and potential mutagenicity of the produced nitro-
72
As an important one-electron oxidant (E0 = 1.23 V18), the contribution from CO3•− to
73
contaminant removal is nonnegligible, which was demonstrated with the treatment of
74
oxytetracycline19, 20 and cylindrospermopsin21. Electron-rich aromatic compounds are preferred
75
for CO3•− attack at relatively high reaction rates, especially phenolic and aromatic amine
76
moieties19, 22, 23. Electron transfer is the dominant route for CO3•−-oxidation, removing an electron
77
from the basic nitrogen atom of an aniline group or from the oxygen atom of a phenolic group to
78
produce a carbonate anion and an aniline/phenol radical cation22-2, 23. H-abstraction for CO3•− is
79
slow24, and radical-addition is not favored due to steric inhibition22. Limited information could be
80
found about the second-order rate constants of CO3•− with CECs20, 21, 25-30. However, few studies
81
evaluated the contribution of CO3•− in removing CECs for water reuse. Moreover, estrone, 17α-
82
ethynylestradiol, diclofenac, triclosan, bisphenol A, and ibuprofen are ranked of high concern for
83
water reuse by a State of California expert panel due to their lack of removal in wastewater
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treatment and their presence at levels that could pose an ecological or human health risk31, 32. For
85
this reason, degradation of these compounds is investigated in this research.
86
The goals of this research are to investigate the influence of alkalinity on UV/NO3−
87
treatment and to provide a fundamental understanding of the selective oxidation of CECs with
88
RNS and CO3•−. The degradation kinetics of selected CECs in the UV/NO3− process with and
89
without HCO3− were evaluated. The second-order rate constants of the selected CECs with CO3•−
90
were determined. Contributions to CEC degradation from UV photolysis, •OH oxidation, CO3•−
91
oxidation, and RNS oxidation were quantified to evaluate the impacts of HCO3−. Transformation
92
products of diclofenac, triclosan, bisphenol A, and estrone in UV/NO3−/HCO3− treatment were
93
detected to elucidate the resulting cytotoxicity of these treated solutions. The RO permeate from
94
the Orange County Water District’ Groundwater Replenishment System (GWRS) was used as a
95
reaction matrix with spiked addition of chemicals (CECs, NO3−, and HCO3−) to assess the
96
applications of UV/NO3−/HCO3− to remove CECs in nitrate/carbonate-rich water reuse scenarios.
97
Experiment Section
98
Chemicals.
99
Eight selected CECs were 17α-ethynylestradiol (EE2), estrone (E1), diclofenac (DCF),
100
triclosan (TCS), bisphenol A (BPA), atrazine (ATZ), carbamazepine (CBZ), and ibuprofen (IBP).
101
Analytical standards were purchased from Sigma-Aldrich at the highest available purity. Their
102
structures and properties are listed in Table 1. RO permeate was collected from the GWRS indirect
103
potable reuse project (April 25, 2017). The GWRS purifies secondary-treated wastewater effluent
104
via chloramination, microfiltration, RO, UV/H2O2, followed by post-treatment stabilization; the
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general water quality parameters of the supplied RO permeate are summarized in Table S1. The
106
other chemicals and reagents used are depicted in Text S1.
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Analysis Methods.
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All contaminants and probe compounds were determined with an 1100 Series HPLC
109
(Agilent) equipped with a diode array detector. A Supelco Discovery C18 HS column (2.1 mm
110
×150 mm, 5 µm) was used before a Poroshell 120 EC-C18 column (2.1 mm × 150 mm, 4 µm) was
111
obtained and utilized. Detailed HPLC conditions may be found in Text S2 and Table S2. The
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concentration of nitrate and chloride ions were determined using a Dionex ion chromatograph with
113
IonPac AS18 column (2 × 250 mm). The mobile phase was comprised of 1.0 mM NaHCO3 and 3.5
114
mM Na2CO3. Concentrations of free chlorine, total chlorine, and monochloramine were
115
determined following the standard analysis methods33.
116
Transformation products of DCF, TCS, BPA, and E1 were detected using an Agilent 1290
117
infinity HPLC with an Agilent 6540 quadrupole time-of-flight mass spectrometer (LC-Q-TOF-
118
MS) at University of Cincinnati, equipped with an Eclipse XDB-C18 column (2.1 mm × 50 mm ×
119
3.5 µm, Agilent ZORBAX). Transformation products of DCF, TCS, BPA were also studied suing
120
an Agilent 6545 LC-Q-TOF-MS with a Poroshell C18 column (2.1 mm × 150 mm × 2.7 µm, Agilent
121
InfinityLab) at University of South Carolina. Transformation products were not measured for EE2
122
due to the similar structure to E1, and were not analyzed for ATZ, CBZ, and IBP either due to the
123
inefficient removal in UV/NO3−/HCO3−. Detailed LC/MS/MS conditions are found in Text S3 and
124
Table S3. Mass spectra were analyzed by Agilent Mass Hunter B.04.00 software.
125
Photochemical Experiments.
126
Photolysis experiments were carried out in a bench scale photochemical apparatus installed
127
with two 15 W low-pressure mercury UV lamps (Cole-Parmer) with monochromatic UV at 254
128
nm. The average UV fluence rate was measured as 0.1 mW cm−2 34. A round Petri dish (60 × 15
129
mm) was used as the reactor, which was covered by a quartz cover (Quartz Scientific Inc., OH) to
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minimized evaporation during the reactions34, 35. A typical experiment was as follows: each tested
131
CEC was spiked into Milli-Q water with an initial concentration of 1 µM and a total volume of 10
132
mL. The initial concentrations of NO3− and HCO3− were added as 10 mM and 3 mM unless
133
specified elsewhere. At different time intervals, 200 µL of the reaction solutions were sampled,
134
quenched with 50 µL of methanol (MeOH), and analyzed by HPLC. No loss of the selected CECs
135
was observed in dark. For detecting the transformation products of DCF, TCS, BPA, and E1, a
136
higher initial concentration was applied. The pH of UV/NO3−/HCO3− process was maintained at
137
8.8 due to the presence of 3 mM HCO3−; borate-boric acid solution (10 mM) was used to stabilize
138
the pH at 8.8 when no HCO3− was added36. The RO permeate water sample was filtered once
139
received and stored at 4 °C if not used immediately. CECs were spiked into RO permeate to test
140
the performance of UV/NO3−/HCO3− within one week of receiving samples. All experiments were
141
performed in triplicate.
142
Determining the Rate Constants for the CECs with CO3•−.
143
Competition kinetic studies were conducted with UV/H2O2 in the presence of 3 mM HCO3−
144
using 1 µM 4-chlorophenol (4-CP) as the reference substance for CO3•− (kCO•3 ― ,4 - CP = 1.9 × 108
145
M−1 s−1)24 and 10 mM tert-butanol (t-BuOH) as the quenching agent for •OH (k•OH,t - BuOH = 6 ×
146
108 M−1 s−1, kCO•3 ― ,t - BuOH < 1.6 × 102 M−1 s−1)12, 37. UV/H2O2 was utilized since the contributions
147
from RNS to the CEC degradation in UV/NO3− and UV/NO3−/HCO3− might be different. The
148
kCO•3 ― ,CEC was calculated using eq. 3, where k'CEC and k'4-CP are the observed degradation rate
149
constants of the selected CEC and 4-CP. The k'CEC and k'4-CP in the UV/H2O2 (1 mM)/t-BuOH (10
150
mM) and UV/H2O2 (1 mM)/HCO3− (3 mM)/t-BuOH (10 mM) system were summarized in Table
151
S4.
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Environmental Science & Technology
k
CO•3 ― ,CEC
= k
CO•3 ― ,4
- CP
×
k'CEC,UV '
k 4 - CP,UV
― H2O2 HCO3 t - BuOH ― H2O2 HCO3 t - BuOH
― k'CEC,UV
H2O2 pH 8.8 buffer t - BuOH
'
― k 4 - CP,UV
(3)
H2O2 pH 8.8 buffer t - BuOH
153
Determining the Steady-State Concentrations of •OH and CO3•−.
154
The concentrations of NO3− were not reduced significantly after the complete removal of
155
CECs under the current conditions (Table S5), therefore, steady-state radical concentrations could
156
be assumed. The steady-state concentration of •OH ([•OH]ss) in the UV/NO3− systems was
157
quantified indirectly by monitoring the degradation of 50 µM of nitrobenzene (NB) as the •OH
158
probe. The depletion of NB by UV only, UV/NO3−, and UV/NO3−/HCO3− was measured by HPLC.
159
Moreover, the degradation of NB with UV/NO3−/10 mM MeOH was almost the same as with UV
160
alone at pH 8.8 (Figure S1), confirming the negligible oxidation of NB by RNS. Therefore, the
161
[•OH]ss in the UV/NO3− system was calculated by using eq. 4.
162
―
163
where kobs is the observed degradation rate constant of NB in the UV/NO3− system, kphotolysis is the
164
observed first-order rate constant of NB under direct UV irradiation, and k•OH,NB (3.9 × 109 M−1
165
s−1)12 is the second-order rate constant of NB with •OH, respectively.
d[NB] dt
= k•OH,NB[•OH]ss[NB] + 0.1 mW cm ―2 × kphotolysis[NB] = kobs[NB]
(4)
166
[•OH]ss was quantified using NB in the UV/NO3−/HCO3− system through eq. 5, since the
167
second-order rate constant of NB with CO3•− (kCO•3 ― ,NB) is lower than 1.3 102 M−1 s−1 23, which
168
is much lower than k•OH, NB. The calculated [•OH]ss was subsequently used to determine [CO•3 ― ]
169
via another probe compound, 4-chlorophenol (4-CP) through eq. 6, which has high rate constants
170
with both •OH (k•OH,4 - CP = 7.6 109 M−1 s−1)12 and CO3•− (kCO•3 ― ,4 - CP = 1.9 108 M−1 s−1)24.
171
Although 4-CP could also react with peroxynitrite, the extremely low second-order rate constant (
172
kPN,4 - CP = 5.1 M−1 s−1)38 made the oxidation by peroxynitrite (PN) negligible in the presence of
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•OH
174
―
175
(5) ―
176
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and CO3•−.
d[NB] dt
'
k•OH,NB[•OH]ss [NB] + kCO•3 ― ,NB[CO•3 ― ]ss[NB] + 0.1 mW cm ―2 × kphotolysis[NB]
=
d[4 - CP] dt
'
= k•OH,4 - CP[•OH]ss [4 - CP] + kCO•3 ― ,4 - CP[CO•3 ― ]ss[4 - CP] +
0.1 mW cm ―2 kphotolysis
(6)
177
[4 - CP] + kPN,4 - CP[PN][4 - CP]
178
where kphotolysis is the observed first-order rate constant of NB/4-CP under direct UV irradiation.
179
Detailed information about calculating [•OH]ss and [CO3•−]ss is shown in Text S4, and degradation
180
of NB and 4-CP are shown in Figure S1 and Figure S2.
181
Calculating the Contributions from UV photolysis, •OH, CO3•−, and RNS.
182
The degradation of CECs by UV/NO3− with or without the addition of HCO3− can be
183
attributed to the direct UV photolysis, •OH oxidation, CO3•− oxidation, and RNS oxidation as
184
shown in eq. 7. ―
185
d[CEC] dt
= 0.1 mW cm ―2 × kphotolysis[CEC] + k•OH,CEC[•OH][CEC] + kCO•3 ― ,CEC[CO•3 ― ] [CEC] (7)
186
+ kRNS,CEC[RNS][CEC]
187
where kphotolysis is the observed first-order rate constant of CEC under direct UV irradiation; and
188
k•OH,CEC, kCO•3 ― ,CEC, and kRNS, CEC represents the second-order rate constant of CEC with •OH,
189
CO3•−, and RNS, respectively. The contributions of each process to CEC degradation was
190
calculated through eq. 8 following the methods previously reported by Fang et al. 39, 40.
191
R=
[CEC]0 ― [CEC]t [CEC]0
t
=
∫0kphotolysis[CEC]dt [CEC]0
t
t
+
∫0k•OH,CEC[•OH][CEC]dt [CEC]0
+
∫0kCO• ― ,CEC[CO•3 ― ][CEC]dt
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[CEC]0
+
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t
192
∫0kRNS,CEC[RNS][CEC]dt [CEC]0
= Rphotolysis + R•OH + RCO•3 ― + RRNS
(8)
193
where R is the fractional removal of the CEC, [CEC]0 is the initial concentration of the CEC, and
194
[CEC]t is the concentration of the CEC at a specific reaction time. The degradation of CECs in
195
UV/NO3− and UV/NO3−/HCO3− can be found in Figure S3. Detailed information about the
196
calculation could be found in Text S5. Table S6 is an example to show the calculations on the
197
contributions from UV, •OH, CO3•−, and RNS to the degradation of DCF in the UV/NO3−/HCO3−
198
process. Results for selected CECs are shown in Figure S4-S5.
199
Cytotoxicity Analysis.
200
Respective cytotoxicity studies for DCF, TCS, E1, and BPA treated by UV/NO3−/HCO3−
201
were carried out using the 3-(4,5-dimethylthiazol-2-yl)-2,5-diphenyltetrazolium bromide (MTT)
202
assay in GeneBLAzer CYP1A1-bla LS-180 cells (Life Technologies, Carlsbad, CA)41. Solid phase
203
extraction (SPE) was used to extract and concentrate samples for cytotoxicity analyses. Details
204
can be found in Text S6. Green (650 nm) and blue (595 nm) absorbance of analytes were measured
205
on a SpectraMax+ 384 plate reader (Molecular Devices, San Jose, CA). The resulting blue: green
206
ratio provides a normalized reporter response, with the higher value indicating lower cytotoxicity.
207
All sample groups were analyzed in triplicate at the concentration of 2.5% MeOH.
208
Results and Discussion
209
CEC Degradation Kinetics in UV/NO3−/HCO3−.
210
The UV fluence-based pseudo-first-order reaction rate constants (kobs) of the eight CECs
211
in different systems at pH 8.8 are compared in Figure 2, namely UV only, UV/HCO3−, UV/NO3−
212
and UV/NO3−/HCO3−. In the absence of HCO3−, only DCF and TCS could be removed by UV
213
only, with a relatively high kobs of 6.0 × 10−3 and 8.0 × 10−3 cm2 mJ−1, respectively. The addition
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of 3 mM HCO3− did not significantly affect the kobs for most of the CECs by UV only. However,
215
the kobs in the presence of 3 mM HCO3− in the UV/NO3− system increased by 61%-177% for CECs
216
with either secondary amine (DCF) or phenolic groups (TCS, E1, EE2, and BPA). For other CECs
217
with weakly electron-donating moieties (ATZ, CBZ, and IBP), kobs decreased by 33%-56%.
218
Through comparing the structure of these eight CECs (Table 1), it was evident that the CECs with
219
phenolic and aniline groups were degraded at a higher rate than other types of CECs with
220
UV/NO3−/HCO3− treatment.
221
Contributions of UV, •OH, CO3•−, and RNS to the CEC Degradation.
222
With the addition of HCO3−, more CO3•− would be formed due to the reaction with •OH5,
223
24.
On the other hand, the scavenging of •OH would lower the Ф(NO2−)3 and enhanced the
224
concentrations of RNS. To further explore the roles of UV, •OH, CO3•−, and RNS on the
225
degradation of E1, EE2, DCF, TCS, BPA, ATZ, CBZ, and IBP in UV/NO3− with or without
226
HCO3−, calculations were conducted following methods reported by Fang et al.39, 40. Steady-state
227
concentrations of •OH and CO3•− in UV/NO3−(10 mM)/HCO3− (3 mM) were assumed and
228
measured as 6.25 10−15 M and 6.91 10−14 M, respectively.
229
UV photolysis. For the selected CECs, only DCF and TCS could be removed at a high rate
230
by direct UV irradiation. The contributions of UV to the removal of DCF and TCS were significant
231
in UV/NO3− and were reduced by 10% and 22% in the presence of HCO3−. UV alone was not able
232
to efficiently decompose other compounds, and thus it made little contribution to their removal,
233
except for ATZ (9%). For these less photo-degradable CECs, the addition of HCO3− did not
234
significantly change the contributions of direct UV photolysis in UV/NO3− at pH 8.8.
235 236
•OH
oxidation. In the absence of HCO3−, ROS (•OH and O2•−) were generated, with a •OH
yield of 9% at 254 nm42. Contributions of O2•− were ignored since O2•− is less reactive than •OH2.
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The removal percentage of the selected CECs ascribed to •OH oxidation was in the range of 5% to
238
41% in UV/NO3− at 172 mJ cm−2 UV fluence (Figure 3). The contribution from •OH-oxidation
239
was directly related to the second-order rate constants of the selected CECs with •OH. E1 has the
240
highest second-order rate constant with •OH, leading to highest removal percentage by •OH
241
oxidation (41%). ATZ and TCS have the low rate constants with •OH, where removal percentages
242
attributable to •OH-oxidation were only 6% and 5%, respectively. For other CECs (BPA, EE2,
243
DCF, IBP, and CBZ) with k•OH,CEC in the range of 7.4 - 10 109 M−1 s−1, the removal percentages
244
attributed to •OH-oxidation were in the range of 12%-20%. Although the second-order rate
245
constants of selected CECs are higher than 109 M−1 s−1, the steady-state concentration of •OH was
246
measured as 1.56 10−14 M with 10 mM NO3−. Thus, the removal percentage of selected CECs
247
due to •OH oxidation was not higher than 41% in UV/NO3− (10 mM).
248
In the presence of HCO3−, the removal percentage of selected CECs due to •OH-oxidation
249
was eliminated to the range of 1% to 9% in UV/NO3− at 172 mJ cm−2 UV fluence (Figure 3). The
250
dominant reason is that the steady-state concentration of •OH was decreased to 6.25 10−15 M in
251
presence of 3 mM HCO3−. However, the overall degradation rate was enhanced by HCO3− for
252
BPA, E1, EE2, TCS, and DCF in the UV/NO3− system. Therefore, the elimination of •OH by
253
adding HCO3− might be the reason of decreased degradation rate for ATZ, CBZ, and IBP, but not
254
the dominant reason for others.
255
CO3•− oxidation. In the absence of HCO3−, the CO3•− can be generated via the reaction of
256
CO2 with ONOO− that is formed during the photolysis of NO3− (eq. 9-10) in alkaline solutions2.
257
Nevertheless, the kCO2,ONOO ― is as low as (2.9 ± 0.3) × 104 M−1 s−1, and the formed adduct,
258
ONOOC(O)O−, decomposes to only 33% NO2• and CO3•− 2. The insignificant amount of CO3•−
259
was not measured and the contributions of CO3•− were negligible for selected CECs in absence of
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HCO3−.
261
ONOO ― + CO2 → ONOOC(O)O ―
262
ONOOC(O)O ― → CO•3 ― + •NO2
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(9) (10)
263
Oxidation reactions with CO3•− are highly selective reactions, as the rate constants range
264
over about 5 orders of magnitude23. Among these investigated CECs, the compounds with phenolic
265
groups exhibited higher rate constants at pH 8.8, including BPA, E1, EE2, and TCS. Noticeably,
266
the kCO•3 ― ,BPA is much higher than the previous reported one, which was determined in UV/Na2CO3
267
using ATZ probe compound27. The difference might be resulted from the extremely low yield of
268
CO3•− in UV/Na2CO3. DCF, which has an aniline group, reacted with CO3•− at a moderate rate of
269
2.7 107 M−1 s−1. For other CECs with weakly electron-donating moieties, such as ATZ, CBZ,
270
and IBP, the second-order rate constants are lower than 107 M−1 s−1. Although the steady-state
271
concentration of CO3•− (6.91 10−14 M) was 10 times higher than that of •OH with the addition of
272
HCO3−, kCO•3 ― ,CEC (106-108 M−1 s−1) of selected CECs are much lower than k•OH,CEC (109-1010 M−1
273
s−1) so that only the removal percentages of BPA, E1, and EE2 ascribable to CO3•− oxidation are
274
visible in Figure 3, while the contributions of CO3•− to remove other CECs are too low to be
275
depicted in the Figure 3. Thus, the elevated concentration of CO3•− in the presence of HCO3− likely
276
contributes to the enhanced degradation rate of BPA, E1, and EE2, rather than for DCF and TCS.
277
RNS oxidation. During the UV photolysis of NO3− at 254 nm, reactive nitrogen species
278
(RNS) were produced, namely ONOO−, •NO2, •NO, NO2−, and peroxynitrite (O2NOO−). Without
279
the addition of HCO3−, EE2 had the largest removal percentage ascribed to RNS (85%), somewhat
280
higher than that of BPA (66%). E1, TCS, and DCF had moderate removal percentages of 21%,
281
29%, and 15%, respectively. RNS contributed to only 5% ATZ degradation, 4% CBZ degradation,
282
and 3% IBP degradation. RNS-based oxidation has preference for CECs with electron-rich
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moieties3, 24, 38. For example, the second-order rate constants with peroxynitrite range from 103 to
284
106 M−1 s−1 1, and the phenolic group is the reactive site for peroxynitrite5, 14, 43. •NO2 can oxidize
285
electron-rich moieties with moderate rate constants, such as phenolic groups, anilines,
286
phenothiazines, and thiols24. The reaction rate constants between most of the RNS and selected
287
CECs are not available due to the complex constituents of NO3− related reactions and the low redox
288
potential (e.g., •NO has an E0 = 0.39 V44). Therefore, the contributions of RNS could not be isolated
289
for each reactive species.
290
In the presence of HCO3−, the removal percentages attributable to RNS enhanced
291
dramatically by 29%, 64%, 37%, and 31% for BPA, E1, TCS, and DCF, respectively. However,
292
the contributions from RNS did not change significantly with the addition of HCO3− for ATZ (-
293
3%), CBZ (-2%), and IPB (3%), respectively. HCO3− affected the RNS species and concentrations
294
via quenching •OH that could minimize the concentration of RNS through eqs. 11-14. In the
295
presence of •OH scavengers, NO2− yields were lowered at pH 83, and ONOO− yields were
296
increased at pH 134, which generates more reactive species, such as •NO2, •NO, and O2•−.
297
Therefore, the change of RNS concentrations should be responsible for the enhancement or
298
reduction of the degradation efficiency of CECs tested when HCO3− was present in the UV/NO3−
299
reaction.
300
•
OH + NO2― → OH ― + •NO2
301
•
OH + •NO2 → ONOOH
302
•
OH + •NO2 → NO3― + H +
(13)
303
•
OH + ONOO ― → OH ― + O2 + •NO
(14)
(11) (12)
304
The Effects of HCO3− in UV/NO3− Treatment.
305
According to the calculations and discussions above, the CECs are classified into three
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groups based on the contributions of UV photolysis, •OH, CO3•−, and RNS in UV/NO3− treatment
307
with the addition of HCO3−. Group I, as less photo-degradable CECs, were primarily decomposed
308
by •OH, CO3•−, and RNS even though they might not have the highest overall removal rate
309
constants. This group include the CECs with phenolic groups, namely BPA, E1, and EE2. They
310
could react rapidly with CO3•− (> 108 M−1 s−1) and RNS5, 14, 43. This group probably contains CECs
311
with aniline moieties, which deserves further exploration.
312
Group II, as photo-degradable CECs, could be efficiently decomposed by direct UV
313
photolysis at 254 nm and RNS. DCF and TCS in this group have electron-rich moieties such as
314
phenolic and aniline groups, which lead to the moderate second-order reaction rate constants (107
315
- 108 M−1 s−1) with CO3•−. However, the removal percentages ascribed to CO3•− oxidation were
316
negligible compared with the significant contributions from RNS and UV photolysis.
317
Group III CECs with weakly electron-donating moieties could not be efficiently removed
318
by UV/NO3− and the degradation rates declined in the presence of HCO3−. CBZ and IBP in this
319
group were primarily degraded by •OH, while the dominant contribution to ATZ removal was UV
320
photolysis.
321
The effects of HCO3− on the degradation of three groups CECs were ascribed to the change
322
of •OH concentrations, RNS speciation, and the formation of CO3•−. On one hand, the •OH
323
concentrations were reduced 10-fold with the continuous generation of CO3•−. The lowered •OH
324
lever affected all kinds of CECs. Since CO3•− reacts more selectively towards phenolic and aniline
325
moieties22,23, the elevated CO3•− concentration contributed to the degradation of the Group I and
326
Group II CECs. On the other hand, the concentrations of ONOO−, •NO2, •NO, and O2•− would be
327
subsequently increased due to the scavenging of •OH. RNS have the inclination to react with CECs
328
with electron-rich moieties at higher reaction rate24-5, 14, 43, significantly affecting the removal of
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Group I and II CECs. The selectivity properties of CO3•− and RNS lead to the inefficient removal
330
of the total organic carbon (TOC) during the degradation of selected CECs.
331 332
Degradation Mechanisms of Diclofenac, Triclosan, Estrone, and Bisphenol A in UV/NO3−/HCO3−.
333
Degradation products detected for TCS, DCF, BPA, and E1 during treatments are
334
summarized in Table S7-S10. The chemical structures of the primary transformation products of
335
TCS, DCF, BPA, and E1 were further supported by MS and MS2 fragmentation using Q-TOF-
336
LC/MS/MS (Figure S6-S12). Isomeric structures for certain products were formed due to the
337
complex oxidation processes, which were observed at different retention time and denoted with a,
338
b, and c. The UV fluence-dependent evolution of transformation products during the degradation
339
of TCS, DCF, and BPA in UV/NO3−/HCO3− can be found in Table S11 and Figure S13-16.
340
Dechlorination-hydrogenation products were observed during TCS degradation in the
341
UV/NO3−/HCO3− process. The transformation product with relatively largest volume was one
342
isomer of dechlorination-hydrogenation products, T253c, (Figure S13), which also was detected at
343
a relatively high volume in the UV-alone system at pH 8.8. Thus, the formation of T253a-c and T264
344
can be attributable to UV photolysis at short wavelength45. Dechlorination-hydroxylation that led
345
to the generation of T235a-c could be initiated by •OH through ipso-attack at the carbon attached to
346
the chlorine (Figure S17a), which has been well-established in the reaction of •OH with
347
halobenzenes46, trimethoprim40, and ATZ47,
348
through the •OH addition, followed by a heterolytic cleavage of the C-Cl bond. Ether-bond
349
breakage was also observed in the process at relatively high UV fluence (> 960 mJ cm−2), leading
350
to T127a, T127b, T161, and T143. Electron transfer through the oxygen atom to •OH/CO3•−/•NO2 led to
351
the formation of a carbon centered radical, undergoing further reaction to break the C1−O bond of
48.
A carbon centered radical was firstly formed
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ether group, which is the weakest site based on the calculation by Gaussian 09 program at
353
B3LYP/6-311+G* level49. The ether-bond can also be broken by •OH attacking on C1 atom through
354
•OH addition-elimination considering the lowest reaction energy barrier of •OH-addition on TCS50.
355
In addition, 2,4-diclophenol (T161) has been detected and identified when TCS was decomposed
356
under irradiation at 316 nm45, confirming the role of UV photolysis to ether-bond cleavage.
357
Interestingly, NO2-adducts, such as T264 and T280, were detected during TCS decomposition
358
which could be ascribed to the contributions of RNS. This route has been proven by the formation
359
of 3-nitrotyrosine through the reaction of tyrosine with •NO2 at a high reaction rate constant (3 ×
360
109 M−1 s−1) (Figure S17b)2. An oxygen-centered phenolic radical was firstly generated via
361
transferring an electron to •OH, CO3•−, or •NO2, followed by the addition of •NO2 radical.
362
Additionally, quinone derivatives, T249, T283, and T317, were observed during the TCS degradation.
363
T303, p-hydroquinone of triclosan, is a common transformation product in •OH-based oxidation
364
process of triclosan, due to the •OH attack at para-position49, 51. Further oxidation of T303 by •OH
365
would lead to the generation of T301, p-quinone of triclosan49, 51. T303 and T301 were not observed
366
during the degradation of TCS in UV/NO3−/HCO3−, which could be ascribed to subsequent
367
formation of T249, T283, and T317 through the dechlorination-hydrogenation, dechlorination-
368
hydroxylation, and hydroxylation routes. Dioxin derivative, T267, was generated through the UV
369
photolysis and •OH oxidation, which raised environmental concern about the toxicity of treated
370
solutions.
371
Cyclization product D260 was detected and identified during DCF decomposition in
372
UV/NO3−/HCO3−. This route was initiated by •OH-induced H-abstraction at C8 as illustrated in
373
Figure S17c45, 52. The formed radical anion subsequently removed a chloride anion at C6 via the
374
dechlorination route to form a biradical under UV irradiation, which leads to a quick recombination
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with the generation of a five-membered cyclic product. Decarboxylation that led to the generation
376
of D216, could be initiated with •OH-involved electron transfer on the carboxylic acid of the D260,
377
which firstly formed a carboxylic radical, followed by removal of CO2 and electron53. No
378
accumulation of D216 was observed possibly due to the further oxidation by •OH or CO3•−,
379
producing a quinine-like product, D214 19, 22, 53-55. Details of decarboxylation are shown in Figure
380
S17d.
381
Hydroxylation was also observed during the BPA degradation with the formation of
382
hydroxylated BPA, B243. Hydroxylation could be initiated with •OH addition as shown in Figure
383
S17e, forming a carbon centered radical, sequentially subjected to oxygen addition, and the
384
removal of perhydroxyl radicals (HOO•)40,
385
undergo CO3•−-initiated addition-elimination route21, the steric inhibition limits the CO3•− addition
386
to the carbon centered radical that formed in the first step22. Considering the activation energy and
387
Gibbs free energy, ortho-hydroxylation was preferred for BPA compared to para-hydroxylation
388
and meta-hydroxylation58. B243 could be further oxidized by •OH to generate the corresponding
389
quinone derivative, B241. B287 is a quinone-like transformation product that has not been reported,
390
which might be generated via further hydroxylation on formed quinone derivatives59. Bond
391
breakage also occurred adjacent to the methyl bridge due to the •OH oxidation with the formation
392
of phenol60, which could react rapidly with •NO2 to produce the product B13857. Interestingly, the
393
concentration of B138 continuously increased with the UV photolysis on NO3− in the presence of
394
HCO3− (Figure S15), even after the completely removal of parent compound, indicating B138 as
395
one of the final oxidation products under current reaction conditions.
56, 57.
Although the hydroxylation was proposed to
396
Hydroxylation played a crucial role during the decomposition of E1 with the formation of
397
transformation product E285a-b, due to the electrophilic attack on the carbon in aromatic ring by
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•OH61.
A quinone product E283 was formed through sequential oxidation of E285 by •OH. E299 was
399
produced as the primary transformation products, with highest amount via the subsequent
400
hydroxylation of E283. Noticeably, NO2-adducts, E314a-b, were also generated during E1
401
degradation in the UV/NO3−/HCO3− process, which was attributable to the contributions of •NO2.
402
Cytotoxicity Studies.
403
The nitro-aromatics that formed during NO3− photolysis might pose a risk on human health
404
and the ecological environment11, 62. Therefore, it is critical to evaluate the cytotoxicity of the
405
resulting treated solution even though Group I and II CECs could be effectively removed by
406
UV/NO3−/HCO3−. In general, the complex reactions of direct photolysis, •OH, CO3•−, and RNS
407
result in complex mixtures of transformation products at low concentration which are difficult to
408
be isolated. Therefore, cytotoxicity of the treated solutions in the UV/NO3−/HCO3− system was
409
evaluated.
410
As shown in Figure 5a, at the beginning stages of DCF degradation, the cytotoxicity
411
declined with decreased DCF (0-160 mJ cm−2 UV fluence). However, the cytotoxicity significantly
412
increased (p = 0.001) after the complete degradation of DCF (> 160 mJ cm−2 UV fluence). The
413
elevated cytotoxicity might be attributed to the accumulation of D260 rather than D214 that was
414
subsequently removed along with the depletion of DCF (Figure S14).
415
Dioxin derivatives observed during the TCS decomposition in the UV/NO3−/HCO3−
416
process, such as T267, possibly have a risk on the ecological and human health11, 50, however, the
417
resulting cytotoxicity analyzed with AhR cells and MTT assays did not significantly change (p =
418
0.264) (Figure 5b). This phenomenon could be ascribed to the rapid degradation of the
419
transformation products (T253, T264, and T314), the low concentrations of the formed transformation
420
products, and the incomplete UV photochemical oxidation of transformation products (T267, and
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T143) within the UV fluence of 640 mJ cm−2 as shown in Figure S13. Similarly, under current
422
reaction conditions (10 mM NO3− and 3 mM HCO3−), no obvious cytotoxicity change was
423
observed (p = 0.426) during the removal of E1 at the UV fluence of 640 mJ cm−2 as shown in
424
Figure 5c.
425
Remarkably, the cytotoxicity of treated BPA decreased (p = 0.067) along with the
426
degradation of BPA (Figure 5d). The generated B243 and B241 were simultaneously removed with
427
BPA, while the formation of nitrophenol (B138) continued to increase in the UV/NO3−/HCO3−
428
system (Figure S15). This result indicates that nitrophenol at low concentration has little effect on
429
the cytotoxicity.
430
Environmental Implications.
431
To evaluate the CEC degradation when NO3− and HCO3− exposed to UV irradiation, RO
432
permeate (UV influent) from GWRS was used as a reaction matrix with spiked additions of
433
chemicals (CECs, NO3−, and HCO3−) to compare the UV/NO3−/HCO3− process with UV only and
434
UV/NO3− methods. Due to the presence of •OH quenching agents such as NO3−, HCO3−, and
435
chloramines63 in the RO permeate (Table S1), the removal of certain CECs with UV/H2O2 was
436
similar with UV only (Figure S18). As shown in Figure 6, the efficiency of three different AOPs
437
was in the order of: UV/NO3−/HCO3− > UV/NO3− > UV only for DCF, TCS, and BPA; and
438
UV/NO3− > UV/NO3−/HCO3− > UV only for ATZ, CBZ, and IBP. These results suggest that higher
439
removal of Group I and Group II CECs by UV/NO3−/HCO3− in RO permeate might be ascribed to
440
the contributions of RNS and CO3•−.
441
This research demonstrates the important role of HCO3− in UV/NO3− treatment,
442
accelerating the removal of Group I and II CECs with electron-rich moieties such as phenolic and
443
aniline groups but inhibiting the destruction of Group III CECs with weakly electron-donating
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moieties. The combined effects of UV photolysis, RNS, •OH, and CO3•− contributed to the
445
degradation of CECs in UV/NO3−/HCO3−. Among the selected CECs, the cytotoxicity was reduced
446
during the BPA degradation in the UV/NO3−/HCO3− treatment. Moreover, the selectivity of RNS
447
and CO3•− made them less affected by NOM and other constituents such as free chlorine and
448
chloramine compared to UV photolysis and UV/H2O2 technologies. Therefore, the residual NO3−
449
and HCO3− in the wastewater have the potential be utilized under UV irradiation for CECs removal
450
in carbonate-rich water reuse scenarios.
451
452
Associated Content
453
Supporting Information
454 455
The Supporting Information is available free of charge on the ACS publications website at http://pubs.acs.org/.
456
Information on chemical used; CECs and transformation products analysis; methodology
457
to determine steady-state concentration of •OH and CO3•−; methodology to calculation
458
contributions on CEC degradation; cytotoxicity analysis methods; water parameters of RO
459
permeate; CO3•− reactions rate constants; LC/MS conditions for transformation products analysis;
460
MS and MS2 spectra for transformation products; UV fluence-based evolution for transformation
461
products during CEC degradation; degradation of NB, 4-CP, and selected CECs (BPA, E1, EE2,
462
TCS, DCF, ATZ, CBZ, and IBP); and additional references. (Text S1-S6, Table S1-S11, and
463
Figure S1-S18).
464
Author Information
465
Corresponding Author
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*Phone: +001- (513) 556-0724; email:
[email protected].
467
Current Address
468
1Department
469
Ohio 45221, USA
470
Notes
471
The authors declare no conflicts of financial interest.
472
Acknowledgements
of Chemical and Environmental Engineering, University of Cincinnati, Cincinnati,
473
The authors acknowledge financial support from the U.S. Geological Survey (USGS)-
474
Water Resources Research Institute (WRRI) (2015SC101G) for this research. Ying Huang
475
acknowledges support from the China Scholarship Council (CSC) scholarship (201306270057).
476
Minghao Kong acknowledges support from the CSC scholarship (201608110134). We are
477
thankful to Orange County Water District for collecting and sending water samples used as a real-
478
world reaction matrix.
479
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Environmental Science & Technology
Table 1. Second-order rate constants for the reaction of CO3•− with the investigated CECs.
pK CEC
Structure a
kCO•3 ― ,CEC at
kCO•3 ― ,CEC
pH = 8.8
(M−1 s−1)
(M−1 s−1)
in ref
k•OH,CEC (M−1 s−1)
Group I: CECs with phenolic moieties O
10. Estrone
(5.3 ± 1.1)
2.6 × 1010
108
64
H
7
H
H
HO
(2.8 ± 0.2) Bisphenol A
1.0 × 1010 0.9) ×
9.6 HO
17α-
(3.89 ±
OH
OH
10.
108
106 65
27
(1.6 ± 0.3)
(9.8 ± 1.2)
108
× 109 66
H
Ethynylestradiol
7
H
H
HO
Group II: photo-degradable CECs OH
Cl
Triclosan
(4.2 ± 1.4)
O
7.9
4.43 × 109 Cl
Cl
COOH Cl
Diclofenac
H N
4.2
107 (2.7 ± 0.7) 8.67 × 109 107
Cl
Group III: CECs with weakly electron-donating moieties Cl
Atrazine
1.6
N
N H
(5.7 ± 0.1)
(3.7-4) ×
106
106 29, 30
2.4 × 109 66
N
N
N H
ACS Paragon Plus Environment
Environmental Science & Technology
13. Carbamazepine
(4.2 ± 0.01)
(2.3-2.5)
(8.8 ± 1.2)
106
× 106 25, 28
× 109 66
(1.2 ± 1.1)
7.89
(7.4 ± 1.2)
106
105 25
× 109 66
N
9
Ibuprofen
Page 34 of 40
O
NH2
OH
4.9 O
678
679
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Environmental Science & Technology
Figure Legends
681
ONOO h
CO2
NO3
h
h O2
+ NO2
NO
h +O
2
h 682 683
NO2
or
h +C O
3
/O
H
+ NO + OH
OH
NO2
+HCO3
H
/O H
+O H
+O
ONOO
CO3
h
Figure 1. Primary reactions during nitrate photolysis at 254 nm in alkalinity solutions.
684 685
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Environmental Science & Technology
UV
30
UV/HCO3UV/NO3UV/NO3-/HCO3-
25 kobs (x 10-2 cm2 mJ-1)
Page 36 of 40
20 15 10 5 0
BPA
E1
EE2
TCS DCF ATZ
CBZ
IBP
686 687
Figure 2. The UV fluence-based pseudo-first-order rate constant (kobs) of CECs in the
688
UV/NO3−/HCO3− processes. [CEC]0 = 1 µM, [NO3−]0 = 10 mM, [HCO3−]0 = 3 mM, pH = 8.8.
689 690
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Environmental Science & Technology
100
UV •OH CO3•− RNS
Removal (%)
80
60
40
20
0 BPA
E1
EE2
TCS
DCF
ATZ
CBZ
IBP
691 692
Figure 3. Removal percentage of CECs by •OH, CO3•−, RNS, and UV during UV/NO3− treatment
693
with (left bar without pattern) and without (right bar with pattern) the addition of HCO3− after the
694
172 mJ cm−2 UV fluence.
695 696
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Environmental Science & Technology
Cl
O
OH
Cl
O
OH
UV
Cl 3
15
Cl
7 8
O
4
5
OH
OH CO3
HO
OH
OH
OH
NO2
OH Cl
Cl
Cl
UV
O HO
Cl
T317, m/z 316.9180 O
OH O
Cl
Cl
Cl O
O
T143, m/z 142.9905
T127a-b, m/z 126.9964
OH
OH
a n UV d
O OH
OH
Cl O
T301
OH
OH
Cl
Cl
Cl O
T303
Cl O
OH
O
OH
UV
O
Cl
OH
Cl
CO3
T161, m/z 160.9597
T280, m/z 280.0005 O
Cl
NO2
Cl
T235,m/z 235.0190
O
Cl
O
NO2
Cl
Cl
T253a-c, m/z 252.9850
OH
OH
O
OH
Cl 17
11
m/z 286.943
OH
T264, m/z 264.0095
NO2
OH Cl
10
6 12
UV
O
UV
9
1
T267, m/z 266.9645
OH
OH
13
2
NO2
Cl
O
Triclosan 14 16
Page 38 of 40
T249, m/z 248.9960
T283, m/z 282.9589
Diclofenac 14
15 6
1
H N
5 4
2
7
12
16
Cl
OH
11
8
Cl
3
COOH
13
17
Cl
H N
COOH
OH
Cl
Cl
H N
N
OH
10
CO3
9
m/z 296.0242
D260, m/z 260.0475
D214, m/z 214.0416
D216
Bisphenol A OH HO
HO
OH
m/z 227.1103
HO
697 698
OH
Estrone
OH
HO
E314a-b, m/z 314.1398
NO2
CO3
O
OH
B138, m/z 138.0211
B287, m/z 287.0558
O
OH
HO
m/z 227.1103
O O
B241, m/z 241.0895
HO
NO2
OH
O
O
OH HO
O O
O
NO2 CO3
HO
OH
B243, m/z 243.1053
O O 2N
OH
O
O
OH
O
E285a-b, m/z 285.1495
E283, m/z 283.1338
O
OH
O
E299, m/z 299.1288
Figure 4. Possible degradation pathways of TCS, DCF, BPA, and E1 in UV/NO3−/HCO3−.
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Environmental Science & Technology
(a) 1.4
0.6
0.2
0.4 0.1
0.0
Normalized absorbance
Normalized absorbance
0.3
0.8
100
200
300
400
500
600
0.3
0.8 0.6
0.2
0.4 0.1
0.2 0.0
0.0 0
0.4
1.0
0.0 0
700
100
1.2
0.3
0.8 0.6
0.2
0.4 0.1
0.2 0.0
0.0 200
300
400
500
400
500
600
700
600
700
0.5
Bisphenol A
0.4
1.0 0.3
0.8 0.6
0.2
0.4 0.1
0.2 0.0
Concentration (mg L -1)
1.0
100
300
1.2 Concentration (mg L -1)
0.4
0
(d) 1.4
0.5
Estrone
Normalized absorbance
(c) 1.4
200
UV fluence (mJ cm-2 )
UV fluence (mJ cm-2 )
700
Concentration (mg L-1)-1)
1.0
Concentration (mg L -1)
0.4
0.2
Normalized absorbance
0.5
Triclosan
1.2
1.2
701
(b) 1.4
0.5
Diclofenac
0.0 0
100
UV fluence (mJ cm-2 )
200
300
400
500
600
700
UV fluence (mJ cm-2 )
702
Figure 5. Cytotoxicity of DCF (a), TCS (b), E1 (c) and BPA (d) treated with UV/NO3−/HCO3−.
703
Left axis represents cytotoxicity by bars; right axis represents concentration by lines. The higher
704
the bar, the lower the toxicity. [CEC]0 = 1 µM, [NO3−]0 = 10 mM, [HCO3−]0 = 3 mM, pH = 8.8.
705
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Environmental Science & Technology
UV
30 k obs (x 10 -3 cm2 mJ -1 )
Page 40 of 40
UV/NO3 UV/NO3 -/HCO3 -
25 20 15 10 5 0 DCF
TCS
BPA
IBP
ATZ
CBZ
706 707
Figure 6. Degradation of spiked CECs by UV/NO3−/HCO3− in the RO permeate from GWRS.
708
[CEC]0 = 1 µM, [NO3−]0 = 10 mM, [HCO3−]0 = 1 mM, pH = 8.0 after the addition of 1 mM HCO3−.
709 710
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