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Transformation of Tetracycline Antibiotics and Fe(II)/(III) Species Induced by Their Complexation Hui Wang, Hong Yao, Peizhe Sun, Desheng Li, and Ching-Hua Huang Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.5b03696 • Publication Date (Web): 30 Nov 2015 Downloaded from http://pubs.acs.org on December 7, 2015
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Environmental Science & Technology
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Transformation of Tetracycline Antibiotics and Fe(II)/(III)
2
Species Induced by Their Complexation
3 4
Hui Wang†,‡, Hong Yao†,§,*, Peizhe Sun‡, Desheng Li†,§ and Ching-Hua Huang‡,*
5 6
†
7
Beijing 100044, Peoples Republic of China
8
‡
9
Georgia 30332, United States
Department of Municipal and Environmental Engineering, Beijing Jiaotong University,
School of Civil and Environmental Engineering, Georgia Institute of Technology, Atlanta,
10
§
11
Beijing Jiaotong University, Beijing 100044, Peoples Republic of China
Beijing Key Laboratory of Aqueous Typical Pollutants Control and Water Quality Safeguard,
12 13 14 15
*
16
*
Phone: 86-10-5168 2157; e-mail:
[email protected] Phone: 404-894-7694; fax: 404-385-7087; e-mail:
[email protected] 17 18 19 20
Revised manuscript submitted to Environmental Science & Technology
21 22
November 27, 2015 1 ACS Paragon Plus Environment
Environmental Science & Technology
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ABSTRACT
24
Tetracycline antibiotics (TCs) are frequently detected micropollutants and are known to have
25
strong tendency to complex with metal ions such as Fe(II) and Fe(III) in the aquatic
26
environment. Experiments with Fe(II) and TCs showed that complexation of Fe(II) with
27
tetracycline (TTC), oxytetracycline (OTC) or chlorotetracycline (CTC) could lead to
28
accelerated oxidation of Fe(II) and promoted degradation of TCs simultaneously. The
29
reaction started with complexation of Fe(II) with TC, followed by oxidation of the Fe(II)-TC
30
complex by dissolved oxygen to generate a Fe(III)-TC complex and reactive oxygen species
31
(ROS). The ROS (primarily ·OH) then degraded TC. The oxidation rate constants of Fe(II) in
32
the FeII-H2L and FeII-HL complexes were 0.269 min-1 and 1.511 min-1, respectively, at
33
ambient conditions (pH 7, 22°C and PO2 0.21 atm), which were about 60 and 350 times of the
34
oxidation rate of uncomplexed Fe(II). Humic acids (HA) compete with TCs for Fe(II) but the
35
effect was negligible at moderate HA concentrations (≤ 10 mg⋅L-1). Experiments with Fe(III)
36
and TCs showed that complexation of Fe(III) with TC could generate oxidized TC and Fe(II)
37
without the need of oxygen, at a relatively slower rate compared to the reaction involving
38
Fe(II), O2 and TCs. These findings indicate the mutually influenced environmental
39
transformation of TCs and Fe(II)/Fe(III) induced by their complexation. These newly
40
identified reactions could play an important role in affecting the environmental fate of TCs
41
and cycling of Fe(II)/Fe(III) in TCs-contaminated water and soil systems.
42 43
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INTRODUCTION
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Tetracycline antibiotics (TCs) are widely used in human medicine, and in livestock and
46
aquaculture industry for controlling diseases and/or promoting growth due to their prominent
47
therapeutic values.1, 2 In 2011, according to the U.S. Food and Drug Administration (FDA),
48
the domestic annual total sales of TCs were at 5,642,573 kg, making them the most selling
49
pharmaceutical group.3 TCs were also reported to be the most widely used antibacterial
50
compounds in the U.K. in 2000 at the usage of 16,268 kg.4 Due to their high usage, TCs may
51
enter the environment through discharge of wastewater effluent and animal manure, leading
52
to potential negative impact on aquatic and terrestrial organisms.4 Recent research has shown
53
the omnipresence of TCs as micropollutants in the environment at the concentrations around
54
4.58 mg⋅kg-1 in animal dung samples, 86-199 µg⋅kg-1 in soils, and 0.13-0.51 µg⋅L-1 in surface
55
waters.5, 6
56
TC compounds, such as tetracycline (TTC), oxytetracycline (OTC) and chlorotetracycline
57
(CTC), consist of a four-ring system with multiple ionizable functional groups (Figure 1).7
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Owing to the multiple O- and N-containing moieties, TCs have a strong tendency to complex
59
with metals,8 which may greatly impact TCs’ fate in the aquatic environment, including
60
interactions with mineral surfaces,9, 10 redox reactions and photodegradation.11, 12 For example,
61
interactions of TTC with metal cations (e.g., Cd(II), Cu(II) and Pb(II)) promoted its
62
adsorption in soils due to ion bridging effects.13 Complexation of TCs with dissolved Mn(II)
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and Cu(II) significantly enhanced TCs’ oxidative transformation in the presence of oxygen at
64
pH 8.0-9.5 and pH 4.0-6.0, respectively.14 Ca(II) and Mg(II) ions in natural water samples
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influenced the direct photolysis11 and self-sensitized oxidation of TCs12 under light irradiation 3 ACS Paragon Plus Environment
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due to formation of Ca(II)- or Mg(II)-TC complexes. Fe(III) ions could bind strongly to TTC
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and act as a photoreactive species in the TTC photodegradation process, affecting the
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photodegradation rate at varying pH.15 Recently, our research team found that complexation
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of TCs with Fe(III) could promote oxidative degradation of TTCs at pH 5-9 without any light
70
exposure. The promoted degradation occurred via complexation of Fe(III) with TCs’
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C4-dimethylamino group and subsequent oxidation by Fe(III) to yield Fe(II) and TC
72
oxidation products.16 However, the impact of Fe(II) on TCs’ transformation had not been
73
investigated.
74
Ferrous ion, as a common form of iron, can be easily oxidized by O2 at neutral pH to form
75
stable Fe(III). Compared to Fe(II), inorganic Fe(III) is highly insoluble, more
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thermodynamically stable, and can be subject to reduction to dissolved Fe(II).17 Fe(II)/Fe(III)
77
is an important redox couple in the natural environment. The transformation between Fe(II)
78
and Fe(III) can occur in the oxic-anoxic boundary of various global reservoirs including
79
atmosphere,18, 19 oceans,20-22 soils,23, 24 and sediments.25-27 In natural waters, most dissolved
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Fe(II) and Fe(III) exist in organic species through organic ligand complexation.28 Some
81
natural or synthetic organic compounds have been observed to accelerate or retard Fe(II)
82
oxidation rate.20, 28-32
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The oxidation of dissolved Fe(II) by ambient O2 (i.e., autoxidation of Fe(II)) has been
84
proposed to consist of four electron transfer reactions shown in eqs 1-4 (the Haber-Weiss
85
mechanism).33 The autoxidation of an organic complex of Fe(II) (i.e., FeII-X, X represents the
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organic ligand) is believed to be similar as shown in eqs 5-9.20, 34
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FeII + O2 → FeIII + O2 ·
-
(1) 4 ACS Paragon Plus Environment
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FeII + O2 · + 2H+ → FeIII + H2 O2
(2)
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FeII + H2 O2 → FeIII + ·OH + OH-
(3)
90
FeII + ·OH → FeIII + OH-
(4)
91
FeII + X ↔ FeII -X
(5)
92
FeII -X + O2 → FeIII -X + O2 ·
93
FeII -X + O2 · + 2H+ → FeIII -X + H2 O2
(7)
94
FeII -X + H2 O2 → FeIII -X + ·OH + OH-
(8)
95
FeII -X + ·OH → FeIII -X + OH-
(9)
-
(6)
-
96
The favorable complexation of TCs to Fe(II) and Fe(III)10, 35, 36 will likely affect the
97
environmental transformation of both TCs and Fe species, but such effects have not been
98
examined thoroughly. Research on the effect of Fe(II) on TCs, in particular, is lacking.
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Therefore, the objective of this study was to investigate the complexation of Fe(II) with TCs
100
and how such complexation influences the transformation of both TCs and Fe(II) under
101
different reaction conditions to elucidate the mechanisms. The impact of Fe(II) was also
102
compared to that of Fe(III) to develop a better understanding of how transformation of TCs
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and redox cycle of Fe(II)/Fe(III) may occur and influence each other simultaneously.
104 105
MATERIALS AND METHODS
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Chemicals and Reagents. TTC, OTC and CTC were obtained from Sigma at 95-97% purity
107
and used directly. Humic acid (HA) was obtained from MP Biomedicals (Santa Ana, CA, US).
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Additional chemicals and reagents used in this study are detailed in the Supporting
109
Information (Text S1). 5 ACS Paragon Plus Environment
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Oxidation Experiments. Unless specified otherwise, all the oxidation experiments were
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conducted by adding 40 µM Fe(II) into 50-mL buffered solution (10 mM buffer of
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2-(N-morpholino)ethanesulfonic acid (MES) for pH 5.5-6.5 or 4-morpholinepropanesulfonic
113
acid (MOPS) for pH 6.5-7.5) in plastic bottles, with magnetic stirring and gentle ultra-zero air
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purging throughout the reaction. The dissolved oxygen (DO) concentration was found to
115
maintain at around 8.9 mg⋅L-1 measured by a DO meter (Orion Star A123, Thermo Scientific).
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The reaction bottles were kept from light. Prior to the reaction, air was bubbled into the
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solution for 5 min to ensure saturated dissolved oxygen before the addition of Fe(II). For the
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oxidation experiments involving both Fe(II) and TCs, different concentrations
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(4.4×103-8.9×104 µg/L or 10-200 µM) of TCs were added into the solution before addition of
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Fe(II). Most experiments were conducted with 40 µM (1.8×104 µg/L) of initial TC
121
concentration. The reactor temperature was maintained at 22 °C. Aliquots were taken
122
periodically from the reaction solution for the determination of Fe(II) and TC concentrations.
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Selected batch reaction experiments were conducted with Fe(III) and TCs, in which the
124
reactors were continuously stirred by a stir bar in the ambient air and protected from light. All
125
the sample aliquots for TCs’ measurements were immediately quenched by adding 0.1 M HCl
126
to reach pH ~2.0. The quenched samples were stored in 2-mL amber glass vials at 5°C and
127
analyzed within 2-3 days. All the experiments were conducted in at least two or more
128
replicates.
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Analytic Methods. Fe(II) concentrations were determined by adding 0.5-mL sample into a
130
cuvette (1.0 cm path length) that contained 0.4-mL 1 mM ferrozine (FZ).37 FZ is known to
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react extremely rapidly and selectively with Fe(II) to form a stable purple complex, Fe(II)FZ3, 6 ACS Paragon Plus Environment
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with maximum absorbance at 562 nm at neutral pH,38-40 and does not bind Fe(III)
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significantly.37, 41 Furthermore, preliminary experiments confirmed that the FZ concentration
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used in this study was sufficient to fully outcompete TCs, resulting in negligible free Fe(II)
135
and Fe(II)-TC complexes (SI Text S2). The absorbance was measured on a Thermo
136
Spectronic Genesys 20 visible spectrophotometer.
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TCs were analyzed by an Agilent 1100 high performance liquid chromatography (HPLC)
138
system with an Agilent Eclipse C18 reverse-phase column (250 mm × 4.6 mm, 5 µm) at 20°C.
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The mobile phase was a mixture of 80% 0.01 M oxalic acid and 20% acetonitrile with a flow
140
rate of 0.8 mL-min-1. TCs were detected at 365 nm by a diode-array UV/vis detector. TCs’
141
transformation products were analyzed by an Agilent 1100 HPLC/UV/MSD system with the
142
same column at a flow rate of 0.5 mL-min-1. Mass spectrometric analysis was conducted by
143
positive electrospray ionization with a mass scan range of m/z 50-1000.
144 145
RESULTS AND DISCUSSION
146
Accelerated Fe(II) Oxidation by TCs. The autoxidation of Fe(II) was significantly
147
enhanced in the presence of TTC (Figure 2), OTC and CTC (SI Figure S1) at pH 6.5.The rate
148
enhancement increased with increasing TC concentration. About 8.9%, 15%, 23% and 36%
149
of Fe(II) were oxidized by O2 in 20 min when the TTC concentrations were 10 µM, 20 µM,
150
30 µM and 40 µM, respectively, whereas only 6.1% of Fe(II) were oxidized in the absence of
151
TCs (Figure 2). The enhancement by the three TCs was comparable, with CTC slightly
152
higher than OTC, followed by TTC. Due to the compounds’ structural similarity and no
153
observed difference in their impact on Fe(II) autoxidation, TTC was chosen as the primary 7 ACS Paragon Plus Environment
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target compound for further experiments. In separate experiments, the solution was purged
155
with nitrogen gas and little transformation of Fe(II) occurred in the presence or absence of
156
TCs (data not shown).
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pH could be an important factor influencing the reaction of Fe(II) autoxidation.42
158
Experiments in the present study showed that the autoxidation rate of Fe(II) increased at
159
higher pH in both the presence and absence of TTC (Figure 3). Very similar trends were also
160
observed for OTC (SI Figure S2). Stumm and Lee demonstrated that the autoxidation rate of
161
inorganic Fe(II) is determined by the concentrations of dissolved oxygen and OH- (eq 10).43
162
The results in Figure 3 and Figure S2 suggest that the oxidation rate of Fe(II) in the presence
163
of TCs follows similar pH dependence as uncomplexed Fe(II).
164
d[FeII] dt
= -k[FeII][O2 ][OH-]
2
(10)
165
Humic acids (HA) are important components of organic matter in natural waters and
166
possess a high density of carboxylate functional groups that may complex with Fe(II). The
167
Fe(II)-carboxylate complexes have faster oxidation rates than inorganic Fe(II) species.20, 31
168
Experiments in the present study showed that the autoxidation rate of Fe(II) increased with
169
increasing HA concentration (SI Figure S3). To assess Fe(II)’s autoxidation in the presence of
170
both TTC and HA, 40 µM TTC was added into solutions containing different concentrations
171
of HA. Results revealed that at lower HA concentrations (5 and 10 mg⋅L-1), the autoxidation
172
rate of Fe(II) was close to the mathematic sum of each alone (Figure 4, SI Figure S4a,b),
173
meaning that at [HA] ≤ 10 mg/L, both TTC and HA promoted the autoxidation of Fe(II)
174
without interference from each other. However, at higher HA concentrations (20 and 40
175
mg⋅L-1), the oxidation rate of Fe(II) approached the oxidation rate in the presence of HA only 8 ACS Paragon Plus Environment
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(Figure 4, SI Figure S4c,d). This was likely caused by the dominance of Fe(II)-HA
177
complexation at a high HA concentration, causing the effect of HA to overshadow the effect
178
of TTC. Hence, HA may only inhibit the effect of TTC on Fe(II) oxidation at high
179
concentrations, suggesting that strong complexation of TCs with Fe(II) plays an important
180
role in systems with low HA concentrations.
181
Evidently, TCs may promote Fe(II)’s autoxidation under most of the reaction conditions
182
tested. In the presence of Fe(II) and TC, the solution contained both Fe(II)-TC complex(es)
183
and free Fe(II), and their relative abundance depended on the concentration ratio of Fe(II) and
184
TC. Several carboxylate organic ligands, including EDTA and citric acid, were reported to
185
accelerate autoxidation of Fe(II) by complexing Fe(II).28-31 The accelerated oxidation rate of
186
Fe(II) by TCs may be due to several possible reasons: (1) the Fe(II)-TC complex(es) are
187
better electron donors and thus more easily oxidized by O2 than uncomplexed Fe(II); (2) TCs
188
may form strong complexes with Fe(III) which subsequently reduce the rate of Fe(II)
189
reformation from Fe(III) reduction; and (3) the intermediate products formed may be strong
190
oxidants of Fe(II).
191 192
Fe(II)-TC Complexation. Complexation of Fe(II) by TCs played a crucial role in the
193
promoted autoxidation of Fe(II). However, the complexation constants of Fe(II) with TCs
194
under environmental conditions were not available in the literature and required further study.
195
Experiments were conducted under anoxic conditions to study the Fe(II)-TC complexation
196
(SI Text S3). The Job’s method has been commonly employed in previous research to
197
determine the stoichiometry and stability constant of certain metal-ligand complex. 44, 45 It 9 ACS Paragon Plus Environment
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was employed in this study to determine the predominant complex species between Fe(II)
199
and TTC at pH 6.5. The Fe(II) and TTC complexation was detected by difference in the UV
200
absorbance of the Fe(II)-TTC complex in comparison to the UV absorbance of the free Fe(II)
201
plus the UV absorbance of free TTC, as shown by eq 11 and Figure S5a:
202
∆Absorbance = Abs (FeII only) + Abs (TTC only) - Abs (FeII + TTC)
203
The ∆(Absorbance) was measured in a series of solutions in which the sum of total Fe(II) and
204
TTC concentration remained the same but their concentration ratio varied. The ∆(Absorbance)
205
was measured immediately after Fe(II) and TTC were mixed together. It was found that the
206
maximum ∆(Absorbance) occurred when the ratio of [Fe(II)]:[TTC] was close to 1 (SI Figure
207
S5b), indicating that the major complex was 1:1 Fe(II)-TTC. Thus, the complexation reaction
208
may be expressed by eq 12:
209
FeII + TTC ⇌ FeII-TTC
210
where [Fe(II)] and [TTC] are the concentrations of uncomplexed Fe(II) and TTC, respectively,
211
and K1:1 is the 1:1 complexation constant.
K1:1 =
[FeII-TTC] TTC[Fe(II)]
(11)
(12)
212
Next, to determine the complexation constant K1:1, the ∆(Absorbance) was measured in a
213
complexometric titration with a fixed total Fe(II) concentration (i.e., Fe(II)T) but varying TTC
214
concentration, and the results were applied to the Benesi-Hildebrand equation (eq 13)45, 46 to
215
obtain the value of K1:1 (details in SI Text S3 and Figure S6) by plotting 1/[TTC] versus
216
1/∆(absorbance), and the complex formation constant could be determined from the slope and
217
the y-axis intercept
218 219
1 ∆(Absorbance)
=
1 Fe(II)T K1:1 ∆ϵ1
×
1 [TTC]
+
1
(13)
Fe(II)T ∆ϵ1
where ∆ϵ1 = ϵ1 - ϵFe(II) - ϵTTC (the molar absorptivity of Fe(II)-TTC complex minus the 10 ACS Paragon Plus Environment
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absorptivities of uncomplexed Fe(II) and uncomplexed TTC). The value of K1:1 was found to vary with pH (SI Text S3), indicating that the speciation of
222
TTC needed to be taken into account in the complexation reaction. As shown in Figure S7,
223
the species of TTC can be expressed as H3L, H2L, HL and L (corresponding to three acid
224
dissociation constants),7 with H2L and HL species dominant in the moderate pH range of 5.5
225
to 7.5 employed in this study (eq 14). Thus, the Fe(II)-TTC complex formation could exist as
226
FeII-H2L and FeII-HL accordingly (eqs 15 and 16):
227
H2 L ⇌ HL + H+
Ka 2 =
228
FeII + H2 L ⇌ FeII -H2 L
KFeII -H2 L =
229
FeII + HL ⇌ FeII -HL
KFeII -HL =
230
Based on the values of K1:1 obtained at different pHs, the complexation constants of KFeII -H2 L
231
and KFeII -HL were determined to be 2.39×103 and 2.05×104, respectively (SI Text S3). These
232
results indicated that, at pH 6.5 for example, about 11% of Fe(II) was complexed with TTC
233
when Fe(II)T:TTCT = 1:1 (TTCT represents total TTC concentration), and the percentage
234
increased to 38% when Fe(II)T:TTCT = 1:5 (SI Text S3 and Figure S8).
HLH+ H2 L
= 10-7.78
(14)
FeII -H2 L H2 L[Fe(II)]
(15)
[FeII -HL] HL[Fe(II)]
(16)
235
Moreover, it was desirable to understand the binding sites of TTC with Fe(II).
236
Complexation of TTC with Fe(II) at varying Fe(II):TTC ratios from 1:4 to 16:4 was
237
measured by UV absorbance spectra immediately after Fe(II) and TTC were mixed together.
238
Thus, any absorbance change was due primarily to complexation and could be calculated
239
using eq 11. The results revealed that the ∆(Absorbance) increased significantly around
240
280-320 nm with an increase in the Fe(II):TC ratio, but did not change as much around
241
340-380 nm (SI Figure S9). Literature has reported that TCs’ A ring (Figure 1) chromophore 11 ACS Paragon Plus Environment
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contributes to the absorption band at 250-300 nm, whereas the BCD ring chromophore
243
contributes to the absorption bands at both 250-300 nm and 340-380 nm.14 Thus, Fe(II) likely
244
complexes with TTC at the A ring and exerts weaker effects on the BCD ring. This result is in
245
agreement with the study by Mikulski et al., which proposed TTC’s amide group and C3
246
oxygen at A ring as the most probable binding site to Fe(II).47
247 248
Oxidation Rate of Fe(II)-TTC Complex. At constant pH and oxygen partial pressure,
249
autoxidation of inorganic Fe(II) species and Fe(II)-organic complexes is expected to follow
250
pseudo-first-order kinetics according to eq 9. Hence, the eq 17 may be used to describe the
251
oxidation of Fe(II) by O2 involving both inorganic Fe(II) species and Fe(II)-organic
252
complexes29, 31, 34:
253
kobs = αi ki + αc kc
254
where kobs (in min-1) is the overall pseudo-first-order oxidation rate constant of Fe(II); αi and
255
αc are the molar fractions of inorganic Fe(II) species and Fe(II)-organic complex, respectively;
256
and ki and kc (in min-1) are the pseudo-first-order oxidation rate constants of the inorganic
257
Fe(II) species and Fe(II)-organic complex, respectively. Note that because the
258
ln{[Fe(II)]t/[Fe(II)]}versus time line was not always straight, the kobs was obtained from a
259
shorter reaction time period where the linear regression yielded R2 ≥ 0.99. The time range
260
was 3 min and 1 min for pH 6.5 and 7.0, respectively.
261
(17)
Since the complexation of Fe(II) with TTC involves FeII-H2L and FeII-HL species, eq 17
262
may be re-written as eq 18:
263
kobs (Fe(II)T ) = ki FeII + kFeII-H2L FeII-H2L + kFeII-HL FeII-HL 12 ACS Paragon Plus Environment
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By combining with eqs 14-16 and the mass balance of total Fe(II), eq 18 is converted to eq
265
19: k obs =
266
ki [Fe(II)] + k FeII -H L [Fe II -H 2 L] + k FeII -HL [Fe II -HL] 2
[Fe(II)] + [Fe II -H 2 L] + [Fe II -HL] ki + k FeII -H L K FeII -H L 2
= 1+
2
K FeII -H L 2
K a2
[H + ] [HL] + k FeII -HL K FeII -HL [HL] K a2
(19)
[H + ][HL] + K FeII -HL [HL]
267
The kobs was measured at a fixed initial Fe(II) concentration but with varying initial TTC
268
concentrations at pH 6.5 and 7.0, respectively (Figure 5, SI Figure S10). Applying the
269
KFeII -H2 L and KFeII -HL values obtained earlier, eq 19 was solved along with the mass balance
270
of total TTC (Text S4) against the kobs data for the unknown kFeII -H2 L and kFeII -HL using
271
Matlab. The kFeII -H2 L and kFeII -HL were calculated to be 0.269 min-1 and 1.511 min-1,
272
respectively, by the model fitting (Figure 5, SI Figure S10, Text S4). The FeII -HL complex’s
273
oxidation rate constant was approximately 5.6 times higher than that of the FeII-H2L complex,
274
indicating that FeII-HL was the major species in promoting Fe(II)’s oxidation in the presence
275
of TTC at near-neutral pH. In comparison, the oxidation rate constant of uncomplexed Fe(II)
276
(ki ) was only 2.60×10-3 min-1 and 4.40×10-3 min-1 at pH 6.5 and 7.0, about 1/100 and 1/600
277
(pH 6.5) or 1/60 and 1/350 (pH 7.0) of that of FeII-H2L and FeII-HL complexes, respectively.
278
Enhanced TTC Degradation. While there was enhancement of Fe(II) autoxidation by TTC,
279
TTC’s degradation was also significantly promoted. For example, 25.6% of 40 µM TTC was
280
degraded in the presence of 40 µM Fe(II) in 90 min at pH 6.5 versus no obvious degradation
281
in the absence of Fe(II) (Figure 6). Furthermore, there was much less degradation of TTC
282
when nitrogen was purged though the solution (Figure 6), indicating that Fe(II)’s autoxidation
283
played an important role in the promoted TTC degradation. Oxidation of Fe(II) could 13 ACS Paragon Plus Environment
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generate Fe(III) and previous research showed that dissolved Fe(III) can complex with TCs
285
and oxidize TCs in the Fe(III)-TC complex.16 However, the Fe(III)-induced degradation of
286
TTC had a much slower rate (less than 6.0% degradation of TTC in 90 min) compared to the
287
Fe(II)-promoted degradation (Figure 6). Thus, the enhanced degradation of TTC by Fe(II)
288
must include other reactions.
289
The Fe(II)’s autoxidation (eqs 1-9) produces three kinds of ROS (O2-·, H2O2, ·OH), which
290
may degrade TTC. To evaluate the role of ROS in both Fe(II) oxidation and TTC degradation,
291
three scavengers (superoxide dismutase (SOD), catalase (CAT), tert-butanol (TBA)) were
292
employed in this study (SI Figure S11). Results showed that addition of the three ROS
293
scavengers had negligible effects on Fe(II)’s oxidation rate in the presence of TTC (Figure
294
7a), indicating that the Fe(II) in Fe(II)-TTC complex was primarily oxidized by dissolved
295
oxygen (eq 6). Conversely, the addition of ROS scavengers affected TTC’s degradation
296
significantly (Figure 7b). TTC degradation was reduced by about 2.68%, 10.0% and 6.60%
297
(at 90 min) when 400 units-mL-1 SOD, 400 units-mL-1 catalase and 1.0 M TBA were added
298
into the solution, respectively. Both catalase (H2O2 scavenger) and TBA (·OH scavenger)
299
retarded TTC’s degradation, indicating that the H2O2 and ·OH formed during Fe(II)-TTC
300
oxidation contributed to TTC’s degradation. This finding is consistent with literature report
301
that TTC can be readily degraded by ·OH radicals at a second-order rate constant of (6.3 ±
302
0.1)×109 M-1s-1.48 In contrast, SOD barely affected TTC’s degradation; this result alone,
303
however, could not exclude the contribution of superoxide radical because SOD may react
304
with O2-· to form H2O2 (eq 20),49, 50 which could react with Fe(II) and TTC subsequently:
305
O2 · + SODFeII + 2H+ → H2O2 + SOD(FeIII)
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306
To verify if O2-· had an effect on TTC’s degradation, higher catalase concentrations and
307
simultaneous addition of both SOD and catalase were tested, respectively. When the catalase
308
concentration was varied from 400 to 2000 units-mL-1, TTC’s degradation decreased from
309
15.6% to 8.2% of that without catalase addition at 90 min. However, further increase of
310
catalase concentration to 4000 units-mL-1 did not result in additional inhibition effect on
311
TTC’s degradation (SI Figure S12a). Thus, the remainder 8.2% enhancement of TTC’s
312
degradation might be caused by O2-· or other reactive species. However, the degradation
313
profile of TTC in the presence of both catalase and SOD overlapped with the profile resulting
314
from the presence of only catalase (SI Figure S12b), which ruled out the impact of O2-· on
315
TTC’s degradation.
316
To further confirm the contribution of H2O2 to TTC’s degradation, three scenarios were
317
tested with addition of H2O2 to solutions containing (1) only TTC; (2) TTC, Fe(III) and TBA;
318
and (3) TTC and Fe(II). In scenario (1), results showed that H2O2 alone had little effect on
319
TTC’s degradation, suggesting that H2O2 cannot directly oxidize TTC. In scenario (2), less
320
than 5% of total TTC was degraded in the H2O2-Fe(III)-TTC system within 90 min (detailed
321
in SI Text S5), which indicated that H2O2 cannot directly oxidize Fe(III)-TTC complex. In
322
scenario (3), the addition of H2O2 with Fe(II), however, significantly enhanced TTC’s
323
degradation due to production of ·OH from the Fenton process (SI Figure S13a), and the
324
oxidation of Fe(II) exhibited the same trend as TTC (SI Figure S13b). Nearly identical
325
concentration consumptions of Fe(II) and TTC were observed in the Fe(II)-TTC-H2O2 system
326
(SI Figure S13c), which also supports that TTC’s degradation is caused by ·OH.
327
Overall, TTC’s degradation during the oxidation of Fe(II) is primarily caused by ·OH. The 15 ACS Paragon Plus Environment
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328
contribution of H2O2 is because it can react with Fe(II) to produce ·OH. Other reactive
329
species (not O2-·) may degrade TTC but at a slight contribution.
330
TTC Degradation Products. Preliminary analyses were conducted to determine the
331
transformation intermediates and products of TTC’s degradation during Fe(II)’s oxidation
332
process. Only one major degradation product was observed on LC/MS; the peak area of the
333
observed product [M+34] (M represents the molecular weight of the protonated parent
334
compound) increased with time (Figure 8a). It was reported that for the ·OH radical reactions
335
with methyl methacrylate, the major reaction pathway involves the addition of ·OH to the
336
terminal carbon of C=C with the breakage of the double bond.51 Thus, the dominant product
337
of [M+34] indicated that there were two oxygen atoms added to the parent compound with
338
the breakage of C=C double bonds, consistent with hydroxylation of TTC by ·OH radicals.
339
OTC and CTC showed similar [M+34] product generation as TTC (data not shown).
340
Moreover, the product’s peak area increased sharply in the first 3 h and then dropped
341
gradually in the following 48 h (Figure 8b). The concentration of Fe(II) dropped to below the
342
method detection limit (MDL) of 0.5 µM in 3.26 h, which could explain why the area of the
343
M+34 product stopped increasing and began to drop. After Fe(II) was depleted, the M+34
344
product was unstable and might be oxidized by Fe(III) formed in the system.
345
Proposed Fe(II)/Fe(III) Redox Cycle in the Presence of TCs and Environmental
346
Implications. On the basis of all of the experimental results, the redox cycle of Fe(II)/Fe(III)
347
in the presence of TCs in aqueous environments is proposed in Figure 9 and the associated
348
reactions and constants listed in Table 1. In the oxic aquatic environment, Fe(III), as the
349
dominated iron species, can complex with TC and oxidizes TC to form Fe(II) and TC radical 16 ACS Paragon Plus Environment
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350
as previously illustrated.16 The yielded Fe(II) can be oxidized back to Fe(III) by oxygen and
351
TC radicals can further degrade. This pathway of Fe(III) and TC transformation is a fairly
352
slow process. On the other hand, in the anoxic aquatic environment, ferrous ions, present as
353
free Fe(II) and Fe(II)-TC complexes, can be easily oxidized to Fe(III) and Fe(III)-TC species
354
when oxygen enters the system. The oxidation rate of total Fe(II) is enhanced by the
355
significantly higher oxidation rate of the Fe(II)-TC complexes. Meanwhile, the ROS
356
(primarily ·OH) formed during Fe(II)’s oxidation induces TC’s degradation. The resultant
357
Fe(III) can be reduced back to Fe(II) by other environmental reductants. More simply, the
358
Fe(II)/Fe(III) redox cycle in the presence of TCs contains two different electron transfer
359
pathways. For the Fe(III)-induced TC degradation process, Fe(III) readily complexes with TC,
360
and the TC molecule acts as the electron donor to Fe(III), forming Fe(II). For the
361
Fe(II)-induced TC degradation process, Fe(II) complexes with TC and the Fe(II)-TC
362
complexes act as the electron donor and transfer electrons to oxygen, forming superoxide
363
anions.
364
The transformation of Fe(II)/Fe(III) may occur in many geochemical environments, such
365
as the oxic/anoxic boundary in marine and freshwater basins, the oxycline in sediments, and
366
sediment-water interfaces.17 TCs, the most widely used antibiotics, enter the aquatic
367
environments via various wastes. When TC contaminants enter the environment, there is a
368
high possibility of TCs and Fe to mutually affect each other’s environmental fate. This study
369
sheds new mechanistic insights on such reactions and improves the knowledge basis to better
370
predict the environmental fate of TC contaminants. Furthermore, this study may provide
371
guidance for additional research on the transformation of transition metal ions and 17 ACS Paragon Plus Environment
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environmental contaminants, as well as facilitate development of remediation strategies for
373
TC contaminants.
374 375
ASSOCIATED CONTENT
376
Supporting Information. Text S1-S5 and Figure S1-S13 are available free of charge via the
377
Internet at http://pubs.acs.org.
378 379
ACKNOWLEDGEMENTS
380
Funding sources of this work included the National Natural Science Foundation of China
381
(51578043), and the U.S. Department of Agriculture Grant 2009-65102-05843. The authors
382
thank the three anonymous reviewers for their helpful comments to improve this manuscript.
383 384
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the
reactions
of
OH
radicals
and
Cl
atoms
517 518
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methyl
methacrylate
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Table 1. Proposed reactions involving Fe(II) or Fe(III) with TCs and associated constants. Stability constant/
Reaction
Ref
Rate constant FeII + H2L ⇌ FeII-H2L
2.39×103a
KFeII-H2L
Complexation
FeII + HL ⇌ FeII-HL
KFeII-HL
FeIII + TC ⇌ FeIII-TC
KFe(III)-TC
FeII + O2 → FeIII + ROS II
e--transfer reaction
105.3, 33
2.05×104a
k0
-
109.9, 33
9.35 M-1⋅min-1a
8.29 M-1⋅min-1,39c
(pH 6.5) 2
-1
(pH 6.5) -1
Fe -H2L + O2 → FeIII-H2L + ROS
k1
9.68×10 M ⋅min
a
-
FeII-HL + O2 → FeIII-HL + ROS
k2
5.44×103 M-1⋅min-1a
-
TTC TTC radical
k3
2.90×10-3 min-1a
-
FeIII-TTC → FeII + TTC radical
k4
1.11×10-4 min-1b
-
FeII, O2
a. Constants determined in this study where pH = 6.5-7.0, T = 22 °C, initial Fe(II)T = TTCT = 40 µM, [O2] = 2.78×10-4 M. b. Constants determined in this study where pH = 7.0, T = 22 °C, initial Fe(III)T = TTCT = 40 µM, solution protected from light. -3
-1
c. The first-order oxidation rate constant of Fe(II) was reported to be 2.33×10 min at pH 6.5, [O2] ~ 2.81×10-4 M and 20.5 °C.
25 ACS Paragon Plus Environment
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R1
R2
pKa1
pKa2
pKa3
Tetracycline (TTC)
H
H
3.32
7.78
9.58
Oxytetracycline (OTC)
H
OH
3.22
7.46
8.94
Chlorotetracycline (CTC)
Cl
H
3.33
7.55
9.33
Figure 1. Structures and properties of TCs.
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1.00
[Fe(II)]t/[Fe(II)]0
0.90
0.80
0.70 w/o TTC w/ 10 µM TTC w/ 20 µM TTC w/ 30 µM TTC w/ 40 µM TTC
0.60
0.50 0
4
8 12 Time (min)
16
20
Figure 2. Effect of initial TTC concentration on Fe(II)’s oxidation in 20 min. Condition: [Fe(II)]0 = 40 µM, pH = 6.5 (buffered by 10 mM MOPS), T = 22 °C, with air purging.
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[Fe(II)]t/[Fe(II)]0
1.00
0.80
0.60 w/o TCs pH 5.5 w/o TCs pH 6.5 w/o TCs pH 7.5 w/ 40 µM TTC pH 5.5 w/ 40 µM TTC pH 6.5 w/ 40 µM TTC pH 7.5
0.40
0.20 0
5
10 15 Time (min)
20
Figure 3. Fe(II)’s oxidation in the absence and presence of TTC at different pH. Condition: [Fe(II)]0 = 40 µM, buffered by 10 mM MES for pH 5.5 and 10 mM MOPS for pH 6.5 and 7.5, T = 22 °C, with air purging.
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0.0
ln{[Fe(II)]t/[Fe(II)]0}
-0.4
-0.8
-1.2
w/ 5 mg/L HA w/ 40 mg/L HA w/ 40 µM TTC w/ 5 mg/L HA + 40 µM TTC w/ 40 mg/L HA + 40 µM TTC sum of 5 mg/L HA and 40 µM TTC sum of 40 mg/L HA and 40 µM TTC
-1.6
-2.0 0
5
10 15 Time (min)
20
Figure 4. Oxidation of Fe(II) in the presence of TTC and HA. Condition: [Fe(II)]0 = [TTC]0 = 40 µM, [HA]0 = 5 or 40 mg/L, pH = 6.5 (buffered by 10 mM MOPS), T = 22 °C, with air purging. Dashed line: the mathematic sum of the effect of HA only and the effect of 40 µM TTC only.
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0.30 0.25
kobs (min-1)
0.20 0.15 0.10 Model fitting
0.05
Experimental data 0.00 0
2
4 6 [TC-] (µM)
8
10
Figure 5. Experimental data and model fitting of observed Fe(II) oxidation rate constants with varying initial TTC concentrations at pH 6.5. Condition: [Fe(II)]0 = 40 µM, [TTC]0 = 0, 40, 60, 90, 120, 150 and 200 µM, buffered by 10 mM MOPS, T = 22 °C, with air purging.
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[TTC]t/[TTC]0
1.00
0.90
0.80 TTC only TTC w/ 40 µM Fe(II), Oxygen TTC w/ 40 µM Fe(II), Nitrogen TTC w/ 40 µM Fe(III)
0.70
0.60 0
30
60 Time (min)
90
Figure 6. Degradation of TTC in the presence of Fe(II) or Fe(III) . Condition: [Fe(II)]0 = [Fe(III)]0 = [TTC]0 = 40 µM, pH = 6.5 (buffered by 10 mM MOPS) and T = 22 °C. Reactions with Fe(II) were purged with air or nitrogen, and no gas purging in the reaction with Fe(III).
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ln{[Fe(II)]t/[Fe(II)]0}
0
-0.2
-0.4 w/o TTC w/ 40 µM TTC, w/o air w/ 40 µM TTC (a) w/ 40 µM TTC, TBA w/ 40 µM TTC, catalase w/ 40 µM TTC, SOD
-0.6
-0.8 0
4
8 12 Time (min)
16
20
[TTC]t/[TTC]0
1.0
0.9
0.8 w/o Fe(II) w/ 40 µM Fe(II) w/ 40 µM Fe(II), TBA w/ 40 µM Fe(II), catalase w/ 40 µM Fe(II), SOD
0.7
(b)
0.6 0
30
60 Time (min)
90
Figure 7. Scavengers’ effects on (a) Fe(II)’s oxidation and (b) TTC’s degradation in the Fe(II)-TTC system. Condition: [Fe(II)]0 = [TTC]0 = 40 µM, pH = 6.5 (buffered by 10 mM MOPS), T = 22 °C, with air purging; [TBA] = 1.0 M, [catalase] = 400 units-mL-1, [SOD] = 400 units-mL-1.
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parent compound product M + 34
12
160
8
120
4
80 (a) 40
Peak Area for M+34 (×105)
Peak Area for parent compound (×105)
16 200
0 0
15
30
45 60 Time (min)
75
90
1
4
[TTC]t/[TTC]0
0.8
product M + 34
3
0.6 2 0.4 [Fe(II)] below MDL
0.2
1 (b)
0
Peak Area for M+34 (×104)
parent compound
0 0
10
20
30
40
50
Time (h)
Figure 8. (a) Product evolution of TTC during Fe(II)’s oxidation process; (b) The evolution of parent TTC and product during Fe(II)’s oxidation process in a 48-hours period. Condition: [Fe(II)]0 = [TTC]0 = 40 µM, pH = 6.5 (buffered by 10 mM MOPS), T = 22 °C, with air purging.
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Figure 9. Proposed Fe(II)/Fe(III) redox cycle in the presence of TC in aquatic environments
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