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Environmental Processes
Chlorate Formation Mechanism in the Presence of Sulfate Radical, Chloride, Bromide and NOM Shaodong Hou, Li Ling, Dionysios D. Dionysiou, Yuru Wang, Jiajia Huang, Kaiheng Guo, Xuchun Li, and Jingyun Fang Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.8b00576 • Publication Date (Web): 10 May 2018 Downloaded from http://pubs.acs.org on May 10, 2018
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Chlorate Formation Mechanism in the Presence of Sulfate Radical, Chloride,
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Bromide and NOM
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Shaodong Houa, Li Lingb, Dionysios D. Dionysiouc, Yuru Wangd, Jiajia Huanga, Kaiheng Guoa,
4
Xuchun Lie, Jingyun Fanga,*
5 6
a. Guangdong Provincial Key Laboratory of Environmental Pollution Control and Remediation
7
Technology, School of Environmental Science and Engineering, Sun Yat-Sen University, Guangzhou
8
510275, China.
9
b. Department of Civil and Environmental Engineering, the Hong Kong University of Science and
10
Technology, Clear Water Bay, Kowloon, Hong Kong
11
c. Environmental Engineering and Science Program, Department of Chemical and Environmental
12
Engineering (DCEE), University of Cincinnati, Cincinnati, OH 45221, USA
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d. Department of Environmental Science, School of Geography and Tourism, Shanxi Normal
14
University, Xi’an 710119, China
15
e. School of Environmental Science and Engineering, Zhejiang Gongshang University, Hangzhou,
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310018, P. R. China
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*Corresponding author. Phone: +86 18680581522; e-mail:
[email protected].
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TOC Art
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Abstract
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Halides and natural organic matter (NOM) are inevitable in aquatic environment and influence the
26
degradation of contaminants in sulfate radical (SO4•‒)-based advanced oxidation processes. This
27
study investigated the formation of chlorate in the co-exposure of SO4•‒, chloride (Cl‒), bromide (Br‒)
28
and/or NOM in UV/persulfate (UV/PDS) and cobalt(II)/peroxymonosulfate (Co/PMS) systems. The
29
formation of chlorate increased with increasing Cl‒ concentration in the UV/PDS system, however,
30
in the Co/PMS system, it initially increased and then decreased. The chlorate formation involved the
31
formation of hypochlorous acid/hypochlorite (HOCl/OCl‒) as an intermediate in both systems. The
32
formation was primarily attributable to SO4•‒ in the UV/PDS system, while Co(III) played a
33
significant role in the oxidation of Cl‒ to HOCl/OCl‒ and SO4•‒ was important for the oxidation of
34
HOCl/OCl‒ to chlorate in the Co/PMS system. The pseudo-first-order rate constants (k′) of the
35
transformation from Cl‒ to HOCl/OCl‒ were 3.32 × 10-6 s-1 and 9.23 × 10-3 s-1 in UV/PDS and
36
Co/PMS, respectively. Meanwhile, k′ of HOCl/OCl‒ to chlorate in UV/PDS and Co/PMS were 2.43 ×
37
10-3 s-1 and 2.70 × 10-4 s-1, respectively. Br‒ completely inhibited the chlorate formation in UV/PDS,
38
but inhibited it by 45.2% in Co/PMS. The k′ of SO4•‒ reacting with Br‒ to form hypobromous
39
acid/hypobromite (HOBr/OBr‒) was calculated to be 378 times higher than that of Cl‒ to HOCl/OCl‒,
40
but the k′ of Co(III) reacting with Br‒ to form HOBr/OBr‒ was comparable to that of Cl‒ to
41
HOCl/OCl‒. NOM also significantly inhibited the chlorate formation, due to the consumption of
42
SO4•‒ and reactive chlorine species (RCS, such as Cl•, ClO• and HOCl/OCl‒). This study
43
demonstrated the formation of chlorate in SO4•‒-based AOPs, which should to be considered in their
44
application in water treatment.
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INTRODUCTION
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Recently, sulfate radical (SO4•‒)-based advanced oxidation processes (AOPs) have attracted
47
increasing attention in both water treatment and groundwater remediation.1 SO4•‒ has a standard
48
reduction potential of 2.5-3.1 V, which is similar or slightly higher than that of hydroxyl radical (HO•)
49
(2.4-2.7 V).1-3 SO4•‒ can be readily produced from the activation of peroxodisulfate (PDS) or
50
peroxymonosulfate (PMS) by UV, heat or transition metals.4-7 Because of its high reactivity and
51
selectivity, SO4•‒-based AOPs have demonstrated their advantages in the destruction of a variety of
52
micropollutants.1 In addition, SO4•‒ has a wider operational pH range and its precursors (i.e. PDS and
53
PMS) are more stable and easier to transport than those of HO• (i.e. peroxide and ozone).4-7 Due to
54
these advantages, SO4•‒-based AOPs have been extensively investigated as an alternative to
55
HO•-based AOPs in some cases for the control of micropollutants such as algal toxins,8, 9 flame
56
retardants,10 pesticides11 and pharmaceuticals5, 7, 12 in water treatment.
57
However, toxic oxidation byproducts, such as bromate and chlorate, are formed in some SO4•‒
58
-based AOPs, due to the inevitable reactions of SO4•‒ with halides in water. Chlorate, a harmful
59
chemical with a health reference level of 210 μg L-1 suggested by U.S. EPA13 and a drinking water
60
standard of 200 μg L-1 regulated in Switzerland,14 can form during the oxidation of chloride (Cl‒) in
61
the UV/PDS system.15 The increase of persulfate dosage and acidic condition favor the formation of
62
chlorate.15 However, the mechanism of chlorate formation from the oxidation of Cl‒ in SO4•‒-based
63
AOPs remains unclear.
64
During the interaction of SO4•‒ with halides, a series of reactive halogen species (RHS) such as
65
halogen atoms (X•), dihalogen anion radical (X2•‒), XO• and free halogen (HOX/OX‒) can be
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generated as eqs 1-6.15-19
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X‒ + SO4•‒ → SO42‒ + X•
(1)
68
X• + X‒ ↔ X2•‒
(2)
69
X2•‒ + X2•‒ → X2 + 2X‒
(3)
70
X2•‒ + X• → X2 + X‒
(4)
71
X2 + H2O → H+ + HOX
(5)
72
X• + HOX → XO•
(6)
73
RHS can be further transformed to halates such as bromate and chlorate through reacting with
74
SO4•‒.20,
75
Bromide (Br‒) can be converted to hypobromous acid/hypobromite (HOBr/OBr‒) as the primary
76
intermediate and to bromate as final product in UV/PDS and Co/PMS systems.20, 21 However, the
77
conversion pathways of Br‒ to HOBr/OBr‒ are different in the two systems. The conversion of Br‒ to
78
HOBr/OBr‒ in the UV/PDS system was primarily driven by SO4•‒,20 while that in the Co/PMS
79
system was driven by Co(III) as the major pathway and by SO4•‒ as the minor pathway.21 The
80
transformation pathways of Cl‒ to chlorate in SO4•‒-based AOPs might share some similarity with
81
that of Br‒ to bromate, but the answers are currently unknown.
21
The formation of bromate in the SO4•‒-based AOPs has been well investigated.20-24
82
In addition, Br‒ and natural organic matter (NOM) are co-present with Cl‒ in natural water, which
83
can affect chlorate formation. The rate constants of Br‒ and NOM reacting with SO4•‒ are 3.5 × 109
84
M-1 s-1 and 2.0 × 103 L mg-1 s-1, respectively. Thus, they can compete with Cl‒ to react with SO4•‒.20,
85
21, 25
86
and HOCl are 1.2 × 1010 M-1 s-1 and (1.55 - 6.84) × 103 M-1 s-1, respectively,26, 27 while the rate
Br‒ and NOM can also react with RHS. For example, the rate constants of Br‒ reacting with Cl•
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constants of NOM reacting with Cl•, ClO• and hypochlorous acid/hypochlorite (HOCl/OCl‒) have
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been reported to be 1.3 × 104 L mg-1 s-1, 4.5 × 104 L mg-1 s-1 and 0.7-5 M-1 s-1, respectively.19, 26, 28
89
Thus, the presence of Br‒ and NOM further make the chemistry of the system more complicated,
90
which influence on the chlorate formation deserves investigation.
91
This study investigated and compared the chlorate formation in UV/PDS and Co/PMS systems,
92
as they are two of the most efficient SO4•‒-based AOPs.4, 6, 10, 12 The objectives of this study were: (1)
93
to investigate the kinetics and mechanisms of chlorate formation from the oxidation of Cl‒ in
94
UV/PDS and Co/PMS processes; (2) to investigate the effects of Br‒ and NOM on chlorate
95
formation.
96 97 98 99
MATERIALS AND METHODS Materials. All chemical solutions were prepared using reagent-grade chemicals and deionized water
(18.2
MΩ
cm)
from
a
Milli-Q
system
(Millipore).
Sodium
persulfate,
100
Oxone®(2KHSO5·KHSO4·K2SO4, 95%), cobalt(II) sulfate heptahydrate (CoSO4·7H2O), N,
101
N-diethyl-p-phenylenediamine (DPD) and fluorobenzene (FB) were purchased from Sigma-Aldrich.
102
Sodium chloride (NaCl), sodium bromide (NaBr), sodium sulfite (Na2SO3) and ethylenediamine
103
tetraacetic acid disodium salt (EDTA) were purchased from Sinopharm Chemical Reagent Co., Ltd
104
(Shanghai, China). Methanol at HPLC grade was obtained from Thermo Fisher. Sodium chlorate
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(NaClO3), potassium bromate (KBrO3), 2,6-dibromophenol (2,6-DBP) and 2,4,6-tribromophenol
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(2,4,6-TBP) were purchased from Aladdin. Suwannee River NOM (Cat. No. 2R101N), obtained
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from International Humic Substances Society, was dissolved in pure water by stirring overnight, and
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was subsequently filtered through a 0.45 μm pore size fiber membrane (Whatman).
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Experimental procedures. For the UV/PDS system, a 700-mL cylindrical, borosilicate glass
110
vessel with a low-pressure mercury UV lamp (254 nm, GPH 135T5 L/4, Heraeus Noblelight) was
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used following Wu et al.29 The unit volume photon flux (I0) entering the solution and the optical path
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length (L) were determined to be 1.45 μEinstein L-1 s-1 using iodide/iodate chemical actinometry,30
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and 3.05 cm by measuring the photolysis rate of H2O2,31 respectively. A water sample containing a
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specific makeup of Cl‒/Br‒/NOM was added to the vessel reactor. PDS at 200 μM was added to the
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reactor and immediately subjected to UV irradiation. For the Co/PMS system, a 250-mL
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batch-reactor was used with mixing provided by a magnetic stirrer. CoSO4, Cl‒/Br‒/NOM and PMS
117
were dosed sequentially in the reactor without any pH adjustment. Samples were taken at
118
predetermined time intervals and divided into two portions. One was immediately subjected to
119
HOX/OX‒ determination. The other was quenched with sodium sulfite for ion chromatography (IC)
120
analysis to measure the concentrations of Cl‒, Br‒, chlorate and bromate. An additional experiment
121
was conducted in the same manner by adding 1 mM FB or 0.2% methanol to the system to study the
122
contributions of Co(III) or SO4•‒ to the formation of HOCl/OCl‒ and chlorate in the Co/PMS system.
123
The solution pH was not adjusted in UV/PDS and Co/PMS systems, which was 4.2 ± 0.2 and 3.8 ±
124
0.2, respectively. All experiments were conducted at ambient temperature and at least duplicated.
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Analytical methods. The concentrations of HOCl/OCl‒ and HOBr/OBr‒ were determined by
126
DPD colorimetric method when either HOCl/OCl‒ or HOBr/OBr‒ was presented alone.32 In the case
127
of the co-presence of HOCl/OCl‒ and HOBr/OBr‒, their total concentrations were determined by
128
DPD colorimetric method, and the concentration of HOBr/OBr‒ was determined following the
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method developed by von Gunten’s group.33 In this method, 2,6-DBP was used to react with
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HOBr/OBr‒ and to produce 2,4,6-TBP with the stoichiometric relationship of 1:1. Then the
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concentration of HOBr/OBr‒ could be quantified by measuring the concentration of 2,4,6-TBP
132
(details in Text S1). The concentration of HOCl/OCl‒ was then calculated by subtracting the
133
concentration of HOBr/OBr‒ from the total halogen concentration. The solution pH was recorded
134
using a Thermo Scientific Orion 420-A pH meter.
135
The concentrations of Cl‒, Br‒, chlorate and bromate were measured by an ion chromatography
136
(IC) system (ICS-900, Dionex) equipped with a conductivity detector. A high-capacity
137
hydroxide-selective analytical column (AS19, 4 × 250 mm, Dionex) with a guard column (AG19, 4
138
× 50 mm, Dionex) was used for separation. A gradient KOH eluent (10 mM initially for 10 min, then
139
ramping to 45 mM from 10 to 25 min) at a flow rate of 1 mL min-1 was provided using an EluGen
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EGC-KOH II cartridge. The injection volume was 250 μL.
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Data simulation. Two kinetic models were conducted to simulate the sequential conversion
142
rates of Cl‒ to HOCl/OCl‒ and then to chlorate by different reactive species in UV/PDS (eqs. 13-18)
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and Co/PMS (eqs. 19-20) systems, respectively, by using Kintecus v5.50.34 The pseudo-first-order
144
rate constants (k′) were determined with the experimental results by the data fitting function of
145
Kintecus v5.50.
146 147
RESULTS AND DISCUSSION
148
Chlorate formation in the co-presence of chloride and SO4•‒. Figure 1a shows the formation
149
of chlorate from the oxidation of Cl‒ in Co/PMS and UV/PDS systems. The yield of chlorate
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increased with increasing reaction time in both systems. While at different Cl‒ dosages, the chlorate
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yield after 30 min, in the Co/PMS system, increased from 5.66 μM to 7.63 μM with increasing Cl‒
152
concentrations from 20 μM to 50 μM at first, and then decreased to 0.559 μM at a Cl‒ concentration
153
of 1 mM. However, in the UV/PDS system, no chlorate was detected when the Cl‒ concentration was
154
lower than 100 μM, while the formation increased from 0.11 μM to 3.27 μM with increasing Cl‒
155
concentration from 100 μM to 1 mM. The conversion rate of Cl‒ to chlorate decreased from 28.3% to
156
0.056% with increasing the Cl‒ concentration from 20 μM to 1 mM in the Co/PMS system, while in
157
the UV/PDS system, it increased from 0.11% to 0.33% with increasing the Cl‒ concentration from
158
100 μM to 1 mM (Figure S1).
159
HOCl/OCl‒ was also generated in the co-presence of Cl‒ and SO4•‒ (Figure 1b). In the Co/PMS
160
system, the yield of HOCl/OCl‒ at 30 min increased from 15.1 μM to 217.5 μM with increasing the
161
Cl‒ concentration from 20 μM to 1 mM. In the UV/PDS system, the yield of HOCl/OCl‒ at 30 min
162
was less than 3.5 μM at a Cl‒ concentration of 1 mM, and was undetectable at 100 μM. The
163
concentration of HOCl/OCl‒ increased with increasing reaction time in both systems when the Cl‒
164
concentration was higher than 50 μM. Moreover, the HOCl/OCl‒ concentration increased firstly and
165
then decreased with increasing reaction time when the Cl‒ concentration was lower than 50 μM in
166
the Co/PMS system (shown in the inset box in Figure 1b), demonstrating that HOCl/OCl‒ might be
167
the intermediate in the conversion of Cl‒ to chlorate.
168
Mechanisms of the chlorate formation in UV/PDS and Co/PMS systems. Figure 2 shows the
169
evolution of Cl‒, HOCl/OCl‒, chlorate and total chlorine (TCl, the total molar masses chlorine in Cl‒,
170
HOCl/OCl‒ and chlorate) during the oxidation of Cl‒ in Co/PMS and UV/PDS systems. In both
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systems, the concentrations of Cl‒ decreased, whereas those of HOCl/OCl‒ and chlorate increased
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with increasing reaction time. TCl remained constant throughout the reaction, demonstrating that
173
HOCl/OCl‒ and chlorate were the major products in both systems. Along with the discussion above
174
(Figure 1), HOCl/OCl‒ can be confirmed to be the key intermediate during the conversion of Cl‒ to
175
chlorate. Therefore, Cl‒ can be converted to HOCl/OCl‒ firstly and finally transformed to chlorate in
176
UV/PDS and Co/PMS systems. Note that the contribution of HO• to the formation of chlorate in this
177
study was insignificant (Text S2).
178
Chlorate formation mechanism in the UV/PDS system. To clarify the roles of SO4•− and UV
179
photolysis on the formation of chlorate in UV/PDS, some additional tests were conducted (Figure
180
S2). In the PDS/Cl‒ system, no HOCl/OCl‒ was formed, demonstrating that Cl‒ could not be oxidized
181
by PDS. The addition of methanol, as a radical scavenger, significantly inhibited the formation of
182
HOCl/OCl‒ in the UV/PDS/Cl‒ system, indicating that SO4•‒ was essential in the conversion of Cl‒ to
183
HOCl/OCl‒. To determine the role of the reactive species attributable to the conversion of
184
HOCl/OCl‒ to chlorate, HOCl was used as the reactant instead of Cl‒ (Figure S2b). The formation of
185
chlorate in the UV/PDS/HOCl system was significantly inhibited by the addition of methanol,
186
indicating that SO4•‒ primarily contributed to the conversion of HOCl/OCl‒ to chlorate. Nevertheless,
187
small amounts of chlorate were still formed in the UV/PDS/HOCl system with the presence of
188
methanol through the UV photolysis of HOCl/OCl‒ (Figure S2b), demonstrating that UV photolysis
189
of HOCl/OCl‒ played a minor role on the chlorate formation. The photolysis of HOCl/OCl‒ formed
190
Cl‒ as the major product and chlorate as the minor product (Figure S3).
191
Chlorate formation mechanism in the Co/PMS system. To ascertain the roles of reactive
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species such as SO4•− and Co(III) on the formation of chlorate in Co/PMS, additional tests were
193
conducted (Figure 3).
194
(1) To ascertain whether Co(III) can oxidize Cl‒ to HOCl/OCl‒ in the Co/PMS system, FB was
195
used to scavenge SO4•‒ (kFB, SO4•‒ = 9.8 × 108 M-1 s-1) but it was less reactive with RHS such as Cl•
196
(kFB, Cl• = 8.0 × 105 M-1 s-1) and HOCl/OCl‒.35, 36 In the Co/PMS/Cl‒/FB system, the formation of
197
HOCl/OCl‒ increased in the first 10 min and then reached a plateau, which was equal to that in the
198
Co/PMS/Cl‒ system in the first 5 min and higher than that thereafter (Figure 3a). The similar
199
HOCl/OCl‒ formation, with or without the presence of FB in the first 5 min indicated that Co(III)
200
played a significant role in the oxidation of Cl‒ to HOCl/OCl‒. The plateau of the HOCl/OCl‒
201
concentration after 10 min demonstrated that SO4•‒ was essential for the oxidation of HOCl/OCl‒ to
202
chlorate in the Co/PMS system.
203
(2) To further ascertain whether Cl• is an important intermediate during the oxidation of Cl‒ to
204
HOCl/OCl‒ by Co(III), methanol was used to scavenge both SO4•‒ and Cl• in the Co/PMS system,
205
with rate constants of 3.2 × 106 M-1 s-1 and 5.7 × 109 M-1 s-1, respectively.36, 37 0.2% methanol (49.4
206
mM) could scavenge both SO4•‒ and Cl• formed in the system. The formation of HOCl/OCl‒ was
207
significantly inhibited in the presence of 0.2% methanol, which was similar to that formed in
208
PMS/Cl‒ (Figure 3a), indicating that Cl• was a key intermediate during the oxidation of Cl‒ to
209
HOCl/OCl‒ by Co(III).
210
(3) In addition, a small amount of HOCl/OCl‒ (1.86 μM) was detected in the PMS/Cl‒ system
211
(Figure 3a), indicating that PMS could directly react with Cl‒ to generate HOCl (eq 7), which was
212
consistent with the literature.38
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Cl‒ + HSO5‒ → SO42‒ + HOCl
214
(4) To determine the role of the reactive species attributable to the conversion of HOCl/OCl‒ to
215
chlorate, HOCl was also used as the reactant instead of Cl‒ (Figure 3b). Chlorate formation was
216
much higher from the oxidation of HOCl than that from Cl−. The formation significantly decreased
217
to only 0.38 μM in the presence of 0.2% methanol in the Co2+/PMS/HOCl system. Note that no
218
chlorate was detected in Co2+/HOCl and PMS/HOCl systems, indicating that neither Co(II) nor PMS
219
could oxidize HOCl/OCl‒ to chlorate. This result indicates that SO4•‒ played a primary role in the
220
oxidation of HOCl/OCl‒ to chlorate, and Co(III) produced from the oxidation of Co(II) had an
221
insignificant contribution to the formation of chlorate.
(7)
222
Proposed pathways of chlorate formation in SO4•‒-based AOPs. Based on the above results
223
and relevant literatures,17, 20, 21, 38, 39 the pathways of chlorate formation in SO4•‒-based AOPs are
224
proposed in Scheme 1. The pathways include the formation of HOCl/OCl‒ as an intermediate and
225
chlorate as the final product. For the first step, SO4•‒, Co(III) and PMS contribute to the formation of
226
HOCl/OCl‒ in different ways. SO4•‒ reacts with Cl‒ to form Cl•, which is subsequently converted to
227
HOCl/OCl‒ through eqs. 8-12.
228
Cl‒ + SO4•‒ → SO42‒ + Cl•
229
Cl• + Cl‒ ↔ Cl2•‒
230
Cl2•‒ + Cl2•‒ → Cl2 + 2Cl‒
231
Cl2•‒ + Cl• → Cl2 + Cl‒
232
Cl2 + H2O → H+ + HOCl + Cl‒
233
k = 3.2 (±0.2) × 108 M-1 s-1
(8)
k+ = 6.5 × 109 M-1 s-1, k- = 1.1 × 105 s-1
(9)
k = 9 (±1) × 106 M-1 s-1
(10)
k = 2.1 (±0.05) × 109 M-1 s-1
(11) (12)
Cl• is also produced by the oxidation of Co(III), and then transformed to HOCl/OCl‒. Meanwhile, a
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small amount of Cl‒ is oxidized to HOCl/OCl‒ by PMS. For the second step, the HOCl/OCl‒
235
produced above is further oxidized by SO4•‒ to generate chlorate as the final product. In addition, the
236
conversion of HOCl/OCl‒ to chlorate by Co(III) is insignificant. UV irradiation plays a minor role in
237
the conversion of HOCl/OCl‒ to chlorate. SO4•‒ pathways outweigh the other pathways among all the
238
steps of chlorate formation in the UV/PDS system. Furthermore, Co(III) plays a more important role
239
in the oxidation from Cl‒ to HOCl/OCl‒, but SO4•‒ is essential for the oxidation from HOCl/OCl‒ to
240
chlorate in the Co/PMS system.
241 242
Scheme 1. Proposed pathways of chlorate formation from the oxidation of Cl‒ in SO4•‒-based AOPs.
243
Conversion Rate Estimation by SO4•‒, UV and Co(III). According to Scheme 1, a model
244
consisting of 6 reactions (eqs 13-18) was constructed by assuming that the two steps conversion of
245
Cl‒ to chlorate (eqs 13-14) by SO4•‒ could be described by pseudo-first-order kinetics in the UV/PDS
246
system.
247 248 249 250 251
SO•− 4
Cl‒ �⎯� HOCl/OCl‒
k1 = ?
(13)
SO•− 4
k2 = ?
(14)
ℎ𝜈𝜈
k3 = 5.52 × 10-6 s-1
(15)
ℎ𝜈𝜈
k4 = 4.76 × 10-4 s-1
(16)
k5 = negligible
(17)
HOCl/OCl‒ �⎯� ClO3‒
HOCl/OCl‒ �� ClO3‒ HOCl/OCl‒ �� Cl‒ ℎ𝜈𝜈
ClO3‒ �� Cl‒
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ℎ𝜈𝜈
ClO3‒ �� HOCl/OCl‒
k6 = negligible
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(18)
253
Where k1 and k2 were fitted with the experimental data in Figure 2a, and k3-k4 were obtained from
254
the results of UV photolysis of HOCl/OCl‒ (Figure S3), with the help of Kintecus v5.50.34 No Cl‒
255
and HOCl/OCl‒ were formed from the UV photolysis of ClO3‒, indicating that k5 and k6 were
256
negligible in the UV/PDS system. As shown in Figure S3, the UV photolysis of HOCl/OCl‒ followed
257
the first-order kinetics, and the rate constants for the formation of ClO3‒ (k3) and Cl‒ (k4) were 5.52 ×
258
10-6 s-1 and 4.76 × 10-4 s-1, respectively (Table S1). The value of k1 and k2 were simulated to be 3.32
259
× 10-6 s-1 and 2.43 × 10-3 s-1, respectively (Table S1). The simulated results were shown in Figure 2a,
260
which were in great agreement with the experimental results, demonstrating that the model and
261
assumptions were reasonable. According to the calculated results, k2 was three orders of magnitude
262
larger than k3, which further proved that the chlorate formation from HOCl/OCl‒ in the UV/PDS
263
system was primarily driven by SO4•‒ and the UV photolysis of HOCl/OCl‒ played a minor role.
264 265 266
As for the Co/PMS system, the stepwise formation of chlorate could be described by eqs 19-20. Co/PMS
Cl‒ �⎯⎯⎯⎯� HOCl/OCl‒ Co/PMS
HOCl/OCl‒ �⎯⎯⎯⎯� ClO3‒
k7 = ?
(19)
k8 = ?
(20)
267
Where k7 and k8 were the pseudo-first-order rate constants of the conversion of Cl‒ to HOCl/OCl‒
268
and the oxidation of HOCl/OCl‒ to chlorate, respectively, in the Co/PMS system. k7 and k8 were
269
simulated to be 9.23 × 10-3 s-1 and 2.70 × 10-4 s-1, respectively (Table S1), by using the experimental
270
data in Figure 1 and the kinetic model.
271
In the UV/PDS system, the SO4•‒- driven rate constant of Cl‒ (1 mM) to HOCl/OCl‒ (3.32 × 10-6
272
s-1) was much lower than that of HOCl/OCl‒ to chlorate (2.43 × 10-3 s-1). Meanwhile, the UV
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photolysis of HOCl/OCl‒ also contributed to the depletion of HOCl/OCl‒ (4.81 × 10-4 s-1) to form
274
Cl‒ as a major product (4.76 × 10-4 s-1) and chlorate as a minor product (5.52 × 10-6 s-1). Thus, the
275
conversion of chloride to HOCl/OCl‒ was a rate limiting step for chlorate formation in UV/PDS,
276
whose kinetics increased with increasing Cl‒ concentration, resulting in the increase of chlorate
277
formation with increasing Cl‒ concentration (Figure 1a). However, in the Co/PMS system, the rate
278
constant of Cl‒ (20 μM) to HOCl/OCl‒ (9.23 × 10-3 s-1) was higher than that of HOCl/OCl‒ to
279
chlorate (2.70 × 10-4 s-1), which led to the significant accumulation of HOCl/OCl‒. Cl‒ has double
280
effects on the formation of chlorate in the Co/PMS system. On one hand, the formation of
281
HOCl/OCl‒ increased with increasing Cl‒ concentration (Figure 1b), which provided more precursors
282
for chlorate formation. On the other hand, the higher concentration of Cl‒ and HOCl/OCl‒ consumed
283
more SO4•‒, resulting in the decrease of the steady-state concentration of SO4•‒ with increasing Cl‒
284
concentration. Thus, the chlorate formation presented a first increase and then decrease trend with
285
increasing Cl‒ concentration in the Co/PMS system (Figure 1a).
286
Effect of bromide on the chlorate formation in the co-presence of chloride, bromide and
287
SO4•‒. In real water, Br‒ and Cl‒ co-exist, and the concentration of the former is much lower than the
288
latter. Figure 4 shows the effect of Br‒ on the chlorate formation in Co/PMS and UV/PDS systems.
289
In the presence of 20 μM Br‒, the formation of chlorate decreased by 45.2% in 30 min in the
290
Co/PMS system at a Cl‒ concentration of 20 μM. Meanwhile, the chlorate formation from 1 mM Cl‒
291
decreased by 100% with the co-presence of 20 μM Br‒ in the UV/PDS system. These results
292
demonstrate that Br‒ significantly inhibits the chlorate formation in both systems, and the inhibition
293
is much higher on the UV/PDS system compared to the Co/PMS system. Br‒ can be oxidized by
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SO4•‒ and Co(III) to form HOBr/OBr‒ and then to form bromate by SO4•‒.20-22 Thus, Br‒ competes
295
with Cl‒ for SO4•‒ or Co(III), resulting in a decrease in chlorate formation, and leads to the formation
296
of bromate in both systems.20, 21 However, the presence of 1 mM Cl‒ did not affect the bromate
297
formation in the UV/PDS system, but the bromate formation decreased by 30.1% in the presence of
298
20 μM Cl‒ in the Co/PMS system after 30 min reaction (Figure S4).
299
In the UV/PDS system, the HOX/OX‒ formation in the co-presence of Cl‒, Br‒ and SO4•‒ are
300
shown in Figure 5a. HOCl/OCl‒ was not detectable in the first 7 min, while its concentration
301
increased with increasing time after 7 min. The concentration of HOBr/OBr‒ firstly increased and
302
then decreased with increasing reaction time. The concentrations of HOCl/OCl‒ and HOBr/OBr‒
303
were 0.1 μM and 5.9 μM, respectively, at 10 min, and the former was much lower than the latter
304
throughout 30 min. As discussed above, the rate constant of Cl‒ to HOCl/OCl‒ was three orders of
305
magnitude lower than that of HOCl/OCl‒ to chlorate in UV/PDS, demonstrating that the limiting step
306
of chlorate formation in UV/PDS was the formation of HOCl/OCl‒. The inhibited formation of
307
HOCl/OCl‒ resulted in the undetectable formation of chlorate in the co-presence of Br‒ and Cl‒ in the
308
UV/PDS system.
309
The inhibition of HOCl/OCl‒ formation and preferential formation of HOBr/OBr‒ (Figure 5a) in
310
the presence of Br‒ is likely attributable to the following aspects. (1) The conversion rate of Br‒ to
311
HOBr/OBr‒ by SO4•‒ is higher than that of Cl‒ to HOCl/OCl‒. The second-order rate constant of
312
SO4•‒ with Br‒ to form Br• (3.5 × 109 M-1 s-1) is around 12 times higher than that with Cl‒ to form
313
Cl• (3.0 × 108 M-1 s-1).3 Furthermore, the transformation rate of Br‒ to HOBr/OBr‒ by SO4•‒ was
314
calculated to be 378 times higher than that of Cl‒ to HOCl/OCl‒, at the same steady-state
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concentration of SO4•‒, by using the kinetic modeling developed by Yang et al. (2014)16 (Details see
316
Text S3 and Figure S5). (2) The reaction rate of Br‒ with Cl• is two orders of magnitude higher than
317
that of Cl‒ with Br• (eqs. 21-22).26 (3) The oxidation of Br‒ by HOCl/OCl‒ with the rate constant of
318
(1.55 - 6.84) ×103 M-1 s-1.27
319
Cl• + Br‒ ↔ BrCl•‒
k+ = 1.2 × 1010 M-1 s-1, k- = 1.9 × 103 s-1
(21)
320
Br• + Cl‒ ↔ BrCl•‒
k+ = 1.0 × 108 M-1 s-1, k- = 6.1 × 104 s-1
(22)
321
As for the Co/PMS system, HOBr/OBr‒ was the primary HOX/OX‒ in the first 1 min and
322
subsequently decreased, accompanied by an increase of HOCl/OCl‒ in the co-presence of Cl‒ and Br‒
323
(Figure 5b). About 96.7% of Br‒ was converted to HOBr/OBr‒ in the first 1 min, followed with a
324
gradual decay of HOBr/OBr‒. The yield of HOBr/OBr‒ in the co-presence of Cl‒ and Br‒ was higher
325
than that of Br‒ alone throughout the reaction period. Meanwhile, the HOCl/OCl‒ formation was
326
retarded compared to that of Cl‒ alone in the Co/PMS system, but they became equal after 7 min. By
327
comparing the cases of Br‒ alone and Cl‒ alone, the accumulation rate of HOCl/OCl‒ was lower than
328
that of HOBr/OBr‒, as was the decay rate after reaching their peak concentrations (Figure 5b).
329
Nevertheless, the conversion of Cl‒ to HOCl/OCl‒ was retarded but still significant in the presence of
330
Br‒, resulting in the formation of chlorate in Co/PMS (Figure 4).
331
The results in Co/PMS are likely to be attributable to the following aspects: (1) The rate
332
constants of the oxidation of Cl‒ to HOCl/OCl‒ (k7 = 9.23 × 10-3 s-1) and the oxidation of HOCl/OCl‒
333
to chlorate (k8 = 2.70 × 10-4 s-1) was lower compared to that of Br‒ to HOBr/OBr‒ (k = 1.48 × 10-2 s-1)
334
and HOBr/OBr‒ to bromate (k = 1.38 × 10-3 s-1) in the Co/PMS system.21 Nevertheless, the
335
conversion of Cl‒ to HOCl/OCl‒ was still significant by Co(III) in the presence of Br‒. (2) Br‒ can
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fast react with HOCl/OCl‒ to form HOBr/OBr‒,27 resulting in the increase of the HOBr/OBr‒ and no
337
HOCl/OCl‒ in the first 1 min. As the reaction proceeded and Br‒ was consumed, HOCl/OCl‒ was
338
accumulated gradually after 1 min.
339
Effect of NOM on the chlorate formation in the co-presence of chloride and SO4•‒. Figure
340
6a shows the effect of NOM on the formation of chlorate in the Co/PMS system. The chlorate
341
formation from 100 μM Cl‒ in 30 min decreased by 83.7%, 95.6% and 99.5% at NOM
342
concentrations of 1 mg L-1, 2 mg L-1 and 5 mg L-1, respectively, in the Co/PMS system. Meanwhile,
343
the chlorate formation was totally inhibited in the presence of NOM in the UV/PDS system. The
344
inhibitory effect of NOM on the chlorate formation is due to: (1) the consumption of SO4•‒ by NOM
345
with a rate constant of 2.0 × 103 L mg-1 s-1;25 (2) the consumption of reactive chlorine species (RCS)
346
such as Cl•, ClO• and HOCl/OCl‒ by NOM with the rate constants of 1.3 × 104 L mg-1 s-1, 4.5 × 104
347
L mg-1 s-1 and 0.7-5 M-1 s-1, respectively.19, 26, 28 The consumption of SO4•‒ and RCS by NOM also
348
resulted in the decreased formation of HOCl/OCl‒. As shown in Figure 6b, the formation of
349
HOCl/OCl‒ from 100 μM Cl‒ in 30 min decreased from 95.8 μM to 30.5 μM with increasing NOM
350
concentration from 0 to 5 mg L-1 in the Co/PMS system. In the UV/PDS system, no HOCl/OCl‒ was
351
detected in the co-presence of 1 mM Cl‒ and 1 mg L-1 NOM.
352
Figure S6 shows the formation of chlorate and HOX/OX‒ in the coexistence of Br‒, NOM and
353
Cl‒ in UV/PDS and Co/PMS systems. In the UV/PDS system, the formation of HOX/OX‒ and
354
chlorate was completely inhibited in the presence of 2 mg L-1 NOM and 20 μM Br‒, similar like that
355
in the presence of Br‒ (Figure 4). In the Co/PMS system, the formation of HOX/OX‒ was inhibited
356
by 50%, with the addition of 2 mg L-1 NOM, while that of chlorate was inhibited by 93.2%,
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compared to the Co/PMS/Cl‒/Br‒ system. This was due to the further consumption of SO4•‒ and RCS
358
by NOM.
359
Engineering Implications. Cl‒ is inevitable in water environment at moderate concentrations
360
of several mg L-1, which concentrations were reported to be 4-11.8 mg L-1 in surface water and 20-30
361
mg L-1 in groundwater.40 The interaction of Cl‒ with SO4•‒ and the formation of chlorate should be
362
taken into consideration during the application of SO4•‒-based AOPs in water treatment.
363
The mechanisms of chlorate formation were different in UV/PDS and Co/PMS AOPs. The
364
former was primarily attributable to SO4•‒ while the latter also involved the contribution of Co(III).
365
The conversion of Cl‒ to HOCl/OCl‒ was the rate limiting step for the chlorate formation in UV/PDS,
366
but that was several orders of magnitude faster in Co/PMS responsible for Co(III). Thus, HOCl/OCl‒
367
was significantly accumulated in Co/PMS, but not in UV/PDS. The accumulation of HOCl/OCl‒
368
consumed SO4•‒ much faster than Cl‒. The above mechanisms resulted in the lower formation rate of
369
chlorate in UV/PDS compared to Co/PMS system at lower Cl‒ concentration (< 0.1 mM), while in
370
opposite at higher Cl‒ concentration (i.e., 1 mM). Meanwhile, the significant accumulation
371
HOCl/OCl‒ in Co/PMS could induce the formation of chlorinated disinfection byproducts (DBPs),
372
particularly at higher Cl‒ concentrations.
373
Water matrices such as NOM, bromide, nitrate and pH affect the formation of chlorate in SO4•‒
374
-based AOPs. Both bromide and NOM reduced the formation of chlorate, but induced the formation
375
of bromate and DBPs, respectively. Nitrate slightly affected the chlorate formation in Co/PMS, while
376
decreased the formation by 35.6% in UV/PDS under the experimental condition (Text S4 and Figure
377
S7). pH affects the chemistry of radicals in SO4•‒-based AOPs and the dissociation of HOCl/OCl‒,
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which may result in the difference of chlorate formation. The formation of chlorate and HOCl/OCl‒
379
at pH 7 were lower than that at pH 4 in both systems (details see Text S5 and Figure S8). Thus, the
380
formation of chlorate in SO4•‒-based AOPs under acidic condition needs more attention.
381 382
ASSOCIATED CONTENT
383
Supporting Information.
384
The Supporting Information is available free of charge on the ACS Publications website.
385
Determination of HOBr/OBr‒ concentrations in the co-presence of HOBr/OBr‒ and HOCl/OCl‒,
386
calculation of HOBr/OBr‒ and HOCl/OCl‒ formation rate by Kintecus at the same steady-state
387
concentration of SO4•‒, the calculated pseudo-first-order rate constants using kinetic models, the
388
contribution of HO• to the formation of chlorate, the conversion rate of Cl‒ to chlorate in Co/PMS
389
and UV/PDS systems, time-dependent HOCl/OCl‒ formation with the presence of methanol and the
390
chlorate formation during the oxidation of HOCl/OCl‒ in the UV/PDS system, formation of Cl‒ and
391
chlorate by direct UV photolysis of HOCl/OCl‒, the formation of bromate in the co-presence of Cl‒
392
and Br‒ in Co/PMS and UV/PDS systems, the formation of chlorate and HOX/OX‒ in the coexist of
393
Br‒, NOM and Cl‒ in Co/PMS and UV/PDS systems, the effect of nitrate and pH on the formation of
394
chlorate and HOCl/OCl‒ in Co/PMS and UV/PDS systems (PDF).
395 396
AUTHOR INFORMATION
397
Corresponding Author.
398
*Phone: + 86-18680581522. E-mail:
[email protected].
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ACKNOWLEDGMENTS
401
This work was financially supported by Natural Science Foundation of China (21677181,
402
51378515), the National Key Research Development Program of China (2016YFC0502803), the
403
Tip-top Scientific and Technical Innovative Youth Talents of Guangdong Special Support Program
404
(2015TQ01Z552), Guangzhou Science Technology and Innovation Commission (201707010249),
405
the Science and Technology Project of Zhejiang Province (2017C33036), and the Fundamental
406
Research Funds for the Central Universities (17lgzd21). D. D. Dionysiou also acknowledges support
407
from the University of Cincinnati through a UNESCO co-Chair Professor position on “Water Access
408
and Sustainability” and the Herman Schneider Professorship in the College of Engineering and
409
Applied Sciences.
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(40) Manna, F.; Cherry, J. A.; McWhorter, D. B.; Parker, B. L. Groundwater recharge assessment in
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an upland sandstone aquifer of southern California. J. Hydrol. 2016, 541, 787-799.
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Lists of Captions Figure 1. The formation of chlorate (a) and HOCl/OCl‒ (b) in Co/PMS (closed symbols) and UV/PDS (open symbols) systems. Conditions: [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [PDS]0 = 200 μM, I0/V = 1.45 μEinstein L-1 s-1. ................................................................................ 2 Figure 2. Evolution of chlorine species during the oxidation of Cl‒ in UV/PDS (a) and Co/PMS (b) systems. Solid lines show simulated results. Conditions: (a) [PDS]0 = 200 μM, [Cl‒]0 = 1 mM, I0/V = 1.45 μEinstein L-1 s-1; (b) [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [Cl‒]0 = 0.1 mM. ........................................................................................................................................ 3 Figure 3. (a) Time-dependent HOCl/OCl‒ formation in the Co/PMS system with the presence of FB or MeOH. (b) Comparison of chlorate formation during the oxidation of HOCl/OCl‒ in different systems. Conditions: [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [Cl‒]0 = 20 μM (a) and 100 μM (b), [FB]0 = 1 mM, MeOH = 0.2%, [EDTA]0 = 20 μM, [HOCl/OCl‒]0 = 100 μM. 4 Figure 4. Effect of Br‒ on the chlorate formation in the Co/PMS (closed symbols) and UV/PDS (open symbols) systems. Conditions: [Co2+]0 = 20 μM, [PMS]0 = 200 μM; [PDS]0 = 200 μM, I0/V = 1.45 μEinstein L-1 s-1. .......................................................................................... 5 Figure 5. Effect of Br‒ on the HOX/OX‒ formation in the UV/PDS (a) and Co/PMS (b) systems. Conditions: (a) [PDS]0 = 200 μM, [Cl‒]0 = 1 mM, [Br‒]0 = 20 μM, I0/V = 1.45 μEinstein L-1 s-1; (b) [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [Cl‒]0 = [Br‒]0 = 20 μM. ............................ 6 Figure 6. The effect of NOM on the formation of chlorate (a) and HOCl/OCl‒ (b) in the Co/PMS system. Conditions: [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [Cl‒]0 = 100 μM. ......... 7
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[Cl-]0 = 20 μM, Co/PMS [Cl-]0 = 50 μM, Co/PMS
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Figure 1. The formation of chlorate (a) and HOCl/OCl‒ (b) in Co/PMS (closed symbols) and UV/PDS (open symbols) systems. Conditions: [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [PDS]0 = 200 μM, I0/V = 1.45 μEinstein L-1 s-1.
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Figure 2. Evolution of chlorine species during the oxidation of Cl‒ in UV/PDS (a) and Co/PMS (b) systems. Solid lines show simulated results. Conditions: (a) [PDS]0 = 200 μM, [Cl‒]0 = 1 mM, I0/V = 1.45 μEinstein L-1 s-1; (b) [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [Cl‒]0 = 0.1 mM.
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Figure 3. (a) Time-dependent HOCl/OCl‒ formation in the Co/PMS system with the presence of FB or MeOH. (b) Comparison of chlorate formation during the oxidation of HOCl/OCl‒ in different systems. Conditions: [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [Cl‒]0 = 20 μM (a) and 100 μM (b), [FB]0 = 1 mM, MeOH = 0.2%, [EDTA]0 = 20 μM, [HOCl/OCl‒]0 = 100 μM.
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Figure 4. Effect of Br‒ on the chlorate formation in the Co/PMS (closed symbols) and UV/PDS (open symbols) systems. Conditions: [Co2+]0 = 20 μM, [PMS]0 = 200 μM; [PDS]0 = 200 μM, I0/V = 1.45 μEinstein L-1 s-1.
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Figure 5. Effect of Br‒ on the HOX/OX‒ formation in the UV/PDS (a) and Co/PMS (b) systems. Conditions: (a) [PDS]0 = 200 μM, [Cl‒]0 = 1 mM, [Br‒]0 = 20 μM, I0/V = 1.45 μEinstein L-1 s-1; (b) [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [Cl‒]0 = [Br‒]0 = 20 μM.
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Figure 6. The effect of NOM on the formation of chlorate (a) and HOCl/OCl‒ (b) in the Co/PMS system. Conditions: [Co2+]0 = 20 μM, [PMS]0 = 200 μM, [Cl‒]0 = 100 μM.
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