Journal Pre-proof Dionysios D. Dionysiou: Funding acquisition; Writing - review and editing.Susceptibility of atrazine photo-degradation in the presence of nitrate: Impact of wavelengths and significant role of reactive nitrogen species Lingjun Bu (Conceptualization) (Data curation) (Software) (Validation) (Writing - original draft), Ningyuan Zhu (Conceptualization) (Writing - original draft), Chunquan Li (Investigation) (Visualization), Ying Huang (Conceptualization), Minghao Kong (Formal analysis) (Writing - review and editing), Xiaodi Duan (Methodology) (Project administration) (Supervision) (Writing - review and editing), Dionysios D. Dionysiou (Funding acquisition) (Writing - review and editing)
PII:
S0304-3894(19)31714-5
DOI:
https://doi.org/10.1016/j.jhazmat.2019.121760
Reference:
HAZMAT 121760
To appear in:
Journal of Hazardous Materials
Received Date:
9 October 2019
Revised Date:
20 November 2019
Accepted Date:
25 November 2019
Please cite this article as: Bu L, Zhu N, Li C, Huang Y, Kong M, Duan X, Dionysiou DD, Dionysios D. Dionysiou: Funding acquisition; Writing - review and editing.Susceptibility of atrazine photo-degradation in the presence of nitrate: Impact of wavelengths and significant role of reactive nitrogen species, Journal of Hazardous Materials (2019), doi: https://doi.org/10.1016/j.jhazmat.2019.121760
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Susceptibility of atrazine photo-degradation in the presence of nitrate: Impact of wavelengths and significant role of reactive nitrogen species
Lingjun Bua, b, 1, Ningyuan Zhub, c, 1, Chunquan Lib, d, Ying Huangb, Minghao Kongb,
a
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Xiaodi Duanb, *, Dionysios D. Dionysioub
Key Laboratory of Building Safety and Energy Efficiency, Ministry of Education,
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Department of Water Engineering and Science, College of Civil Engineering, Hunan University, Changsha, 410082, China
Department of Chemical and Environmental Engineering, 705 Engineering Research
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b
Center, University of Cincinnati, Cincinnati, OH 45221-0012, USA c
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Zigui Ecological Station for Three Gorges Dam Project, State Key Laboratory of Soil
and Sustainable Agriculture, Institute of Soil Sciences, Chinese Academy of Sciences,
d
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71 East Beijing Road, Nanjing 210008, China
School of Chemical and Environmental Engineering, China University of Mining and
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Technology (Beijing), Beijing 100083, PR China
*
Corresponding author: Xiaodi Duan (
[email protected])
1
These authors contributed equally to this work and shared co-first authorship.
Graphical absctract
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Highlights
RNS are major contributor to degradation of ATZ in UV285/nitrate.
RNS are helpful to accelerate the photo-transformation of ATZ.
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Abstract
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The influence of UV light wavelengths on degradation of ATZ was investigated. UV285/nitrate showed better performance than UV255/nitrate.
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The role of reactive nitrogen species (RNS) formed from nitrate photolysis has aroused interests in transformation of contaminants of emerging concern. This study
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investigated the influence of UV wavelengths (255, 285 and 365 nm) on photolysis of nitrate for degradation of atrazine (ATZ). The UV285/nitrate system showed the fastest rate constant for degradation of ATZ with kobs of 0.0022 cm2 mJ-1. UV photolysis, RNS, and hydroxyl radical (HO•) were identified as main contributors to ATZ degradation in UV/nitrate system. Among the contributors, RNS made the major contribution to degradation of ATZ in UV285/nitrate system, while HO• is the predominant specie in
UV255/nitrate system. Variance decomposition analysis showed that degradation of ATZ was slightly impacted by natural organic matter and carbonate/bicarbonate in UV285/nitrate system but was dramatically affected in UV255/nitrate system. Main transformation products of ATZ in UV285/nitrate system were identified and possible pathways were proposed. RNS were confirmed to be favorable for acceleration of ATZ photolysis through further reaction of RNS with hydroxyatrazine (with electron-rich moieties). Our study provides deep insights on the influence of UV wavelength on
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nitrate photolysis and ATZ degradation, and provides a novel method for remediation of water co-contaminated by nitrate and organic contaminants.
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Keywords: UV wavelength; nitrate photolysis; atrazine; reactive nitrogen species.
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1. Introduction
Nitrate (NO3−) photolysis has received great attention in past decades because the
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ubiquitous NO3− is a main source of reactive radicals in natural waters in the presence of solar light [1]. Although the nitrate photolysis may pose health risks in water
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purification because of the formation of nitro-derived compounds [2], researchers has proven the important role of photolyzed nitrate in the degradation of contaminants of
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emerging concern (CECs) [3-5]. Photolysis of nitrate could produce hydroxyl radicals (HO•) and reactive nitrogen species (RNS) (Eqs. 1-4), such as nitrogen dioxide radical (NO2•), nitrite (NO2−), O(3P), and peroxynitrite (ONOO−) [6-9]. The photolyzed pathways of nitrate have been intensively and thoroughly investigated at different light wavelengths [9, 10]. However, the impact of light wavelengths on nitrate photolysis associated with degradation of contaminant has not been previously investigated in
depth. NO3− + hv → NO2• + O•−
(1)
O•− + H2O → HO• + OH−
(2)
NO3− + hv → NO2− + O(3P)
(3)
NO2• + HO• → HOONO
(4)
NO2− + HO• → NO2• + OH−
(5)
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Among the products of photolyzed nitrate, HO• and RNS have been confirmed to
possess the potential to attack CECs [3, 5]. The quantum yields of HO• from nitrate photolysis was reported to be higher at short wavelengths: around 9% at UV254, and
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declined steadily to 1% with the wavelength increasing to 300 nm and above [9, 11]. However, the generated HO• (E0 = 2.0 V) [12] could be quenched by other products of
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photolyzed nitrate, such as nitrite or NO2• (Eqs 4-5) [9], and usually be quenched by
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carbonate/bicarbonate ions and organic matters, limiting the reactions between HO• and target contaminants [13]. Taking NO2• (E0 = 1.03 V) [14] as an example, RNS are
[3, 15].
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usually selective and can react rapidly with contaminants with electron-rich moieties
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Atrazine (ATZ), as one of the triazine herbicides, has received much attention because of the continually increasing consumption in agriculture field and the
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potentially toxic impacts when leaching into aquatic ecosystems [16, 17]. Former research studies showed that photo-transformation of ATZ was an important pathway for ATZ removal, which was hardly affected by the wavelength of light source [18]. However, direct photolysis of ATZ is inadequate because the main intermediate products (hydroxyatrazine and 4-ethylamino-6-isopropylamino-2-hydroxy-s-triazine) are inert for further photolysis [19]. Notably, ATZ and nitrate are simultaneously
present in agricultural runoffs which causes widely pollution in surface waters [20, 21]. Therefore, the generated HO• and RNS from the photolysis of nitrate (eqs. 1-5) can efficiently degrade the co-existed ATZ, and RNS mainly remove ATZ via electrophilic substitution. Nitrate often exists in agricultural runoffs at concentrations up to 0.6 mM [13]. Only few research studies have focused on the photochemical removal of ATZ in the presence of nitrate [3, 19], especially on the role of RNS because of the electrondonated nature of ATZ. Also, investigations on the degradation of ATZ using different
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light wavelengths in the presence of nitrate can provide new insights for remediation of ATZ-polluted water.
Thus, this study aims to 1) investigate the impact of light wavelength on nitrate
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photolysis for ATZ degradation; 2) evaluate the contributions of RNS on ATZ
degradation in the presence of nitrate.
2.1 Photolysis experiments
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2. Materials and Methods
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degradation and 3) explore the possible degradation mechanisms involved during ATZ
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Photolysis experiments were carried out with collimated UV-LEDs (255 nm, 0.03 mW cm−2; 285 nm, 0.12 mW cm−2; and 365 nm, 3.05 mW cm−2, Pearlbeam, AquiSense
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Technologies, KY) in a laboratory scale system. The UV intensity was determined by
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ferrioxalate actinometry method reported in our previous study [22]. In a typical experiment, solutions were prepared with 1 μM of ATZ and 4 mM nitrate with a total volume of 10 mL in a petri dish (60 × 15 mm) with a quartz cover (Quartz Scientific Inc., OH), unless stated otherwise. All experiments were performed in triplicates at ambient temperatures (21 ± 1 °C). The reaction was initiated by collimated UV-LEDs illumination of individual of beam. At different time intervals, 200 μL of solution
samples were collected and quenched by 50 μL methanol (MeOH) for further analysis. After reaction, the samples were taken to analyze the concentration of nitrate and nitrite. All chemicals used in this study were of analytical grade purity and were obtained from Sigma-Aldrich. In another set of experiments, direct ATZ photolysis was detected in the same reactor with the same light conditions as above mentioned. The solution only composed of 10 mL of ATZ with the concentration of 1 μM.
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To evaluate the ATZ degradation performance in natural water, filtered water
samples were collected from Lao Yinggou River (Yichang, Hubei). Experiments were carried out as the same procedures mentioned above in collected water samples with
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spiked chemicals. To distinguish the influence of initial concentration of nitrate, initial
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pH, natural organic matters (NOM) and bicarbonate/carbonate on ATZ degradation by nitrate photolysis, experiments were conducted with the same conditions mentioned
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above. To explore the influence of initial concentration of nitrate, ATZ was also treated at the nitrate concentration ranging from 0 to 10 mM (0, 0.2, 2, 4, 6, 10 mM). Besides,
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to evaluate the influence of pH, experiments were carried out at pH ranging from 4.0 to 8.5 which was adjusted by 0.05 M H2SO4 or 0.1 M NaOH. Different dosages of NOM
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(from Suwannee River, supplied by international humic substances society, 0-10 mg-C L-1) and NaHCO3 (0, 50, 100, 150, 200 mg L-1) were added to the reactor, respectively,
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to investigate the influence of NOM and alkalinity. 2.2 Contributions of reactive species In UV/nitrate system, direct UV photolysis, oxidation by HO• or RNS could result in the degradation of ATZ as follow: −
d[ATZ] dt
= Li × k photolysis [ATZ] + k HO•ATZ [HO• ][ATZ] + k RNS,ATZ [RNS][ATZ] (6)
where Li is the light intensity, kphotolysis represents the reaction rate calculated from ATZ degradation by direct UV irradiation, kHO•,ATZ and kRNS,ATZ are the second-order rate constants of ATZ with HO• and RNS, respectively. The steady-state concentration of HO• ([HO•]ss) was then estimated because the concentration of nitrate changed slightly before and after reaction according to Huang et al.’s method [3]. Nitrobenzene (NB), an effective hydroxyl radical scavenger with known rate constants [22], was selected as the HO• probe because of the negligible degradation by RNS. The degradation of 50
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μM of NB by direct UV photolysis and UV/nitrate at different wavelengths were measured by HPLC. Thus, the [HO•]ss was then calculated following Eq. (8): d[NB] dt
= Li × k photolysis [NB] + k HO• ,NB [HO• ]ss [NB] = k obs [NB]
(7)
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−
where the Li is the light intensity, kphotolysis represents the reaction rate of direct UV
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degradation of NB, k HO• ,NB (the second-order rate constant of NB with HO•) is 3.9 × 109 M-1 s-1 [12]. The degradation curves of NB by UV255/nitrate, UV255 irradiation,
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UV285/nitrate, UV285 irradiation are presented in Figure S1. The [HO•]ss was calculated after knowing the value for kphotolysis related to NB degradation (Table S1). Then, the
R= 𝑡
𝑡
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as follows:
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contribution of UV photolysis, HO• and RNS on ATZ degradation could be calculated
[𝐴𝑇𝑍]0 −[𝐴𝑇𝑍]𝑡 𝐴𝑇𝑍0
=
∫0 𝑘𝑝ℎ𝑜𝑡𝑜𝑙𝑦𝑠𝑖𝑠 [𝐴𝑇𝑍]𝑑𝑡
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∫0 kRNS,ATZ [𝑅𝑁𝑆][𝐴𝑇𝑍]𝑑𝑡 𝐴𝑇𝑍0
𝐴𝑇𝑍0
𝑡
+
∫0 kHO• ATZ [𝐻𝑂• ][𝐴𝑇𝑍]𝑑𝑡 𝐴𝑇𝑍0
+
= 𝑅𝑝ℎ𝑜𝑡𝑜𝑙𝑦𝑠𝑖𝑠 + 𝑅𝐻𝑂• +𝑅𝑅𝑁𝑆
(8)
where R is the removal of ATZ from different contributors, [ATZ]0 is the initial
concentration of ATZ, and [ATZ]t is the concentration of ATZ at a given time t. The detailed information about the calculation is presented in Table 1. 2.3 Analytical methods and statistics
The concentration of ATZ was determined by High Performance Liquid Chromatography (HPLC, Agilent1100 Series). The Agilent 1260 infinity HPLC, equipped with an Eclipse XDB-C18 column (2.1 mm × 50 mm × 3.5 μm, Agilent ZORBAX), with an Agilent 6420 triple quadrupole mass spectrometer (LC-MS) was used to analyze the transformation products of ATZ. Mass spectra were analyzed by Agilent Mass Hunter B.04.00 software. The variation of toxicity during the treatment was experimentally monitored using bacterial luminescence Vibrio fischeri (strain Nitrate
and
nitrite
concentrations
were
determined
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NRRL-B-11177).
spectrophotometrically based on Brucine-sulfanil colorimetric method [23] and Griess
Assay reaction [24], respectively, using a double UV-vis Spectrophotometer (UV-2450
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Shimadzu, Japan) [25].
Variance partition analysis (VPA) was performed to distinguish the role of
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different natural components (concentration of nitrate, dissolved organic carbon, pH,
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carbonate/bicarbonate) on ATZ degradation by UV/nitrate at different wavelengths. These analyses were performed using R software with vegan package (the detailed
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running script was supplied in SI Text S1). One-way AVONA was used for statistical analysis and the probability value was set at 0.05 level for all analyses.
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3. Results and Discussion
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3.1 Degradation of ATZ by photolysis of nitrate The degradation of ATZ (1 μM) by UV-LEDs with different radiation wavelengths
(255, 285 and 365 nm) in the presence of nitrate was investigated in a series of experiments. As shown in Figure 1a, 87.7% of ATZ was removed after 120 min irradiation by UV285 whereas UV255 and UV365 eliminated no more than 12% ATZ in the presence of nitrate. The time-based pseudo-first order rate constants (ktobs) of ATZ
degradation were 0.0008 min-1, 0.0158 min-1, 0.0005 min-1 for UV255, 285 and 365 nm, respectively (Figure S2). The UV fluence based pseudo-first order rate constants (kfobs) were then calculated in consideration of the influence of intensities [26]. The kfobs for UV285 was 0.0022 cm2 mJ−1 which was 7.3 times compared to that of UV255 in the presence of nitrate. UV365 was not studied in the following sections because the kfobs for UV365 (0.0002 cm2 mJ−1) was much lower than that of UV285. Meanwhile, direct photolysis of ATZ in the absence of nitrate was also considered: UV285 showed a better
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performance on the degradation of ATZ than UV255 in sole photolysis process (Figure S3), suggesting that UVB (285 nm) irradiation was more effective to decompose ATZ in the absence or presence of nitrate. Of note, the UV adsorption spectrum of nitrate
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has two peaks at ~200 nm band (190 to 250 nm) and ~300 nm band (270 to 330 nm),
respectively [9, 10]. As known, the wavelength of solar light reaching down to the
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terrestrial surface waters is above 290 nm [27]. Thus, this study shows the feasibility of
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nitrate responses to ~300 nm band irradiation for transformation of organic contaminants. We also investigated ATZ degradation by photolysis of nitrate under UVvis light (300-760 nm), which also resulted in 35.3% ATZ removal (Figure S4). Among
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the photolysis products of nitrate, the HO• and RNS (mainly NO• and N2O•) could result in degradation of organic contaminants [3]. As referred above, the quantum yield of
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HO• from nitrate photolysis at UV255 is much higher than that of UV285 [8, 28]. However,
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this study showed a much more effective degradation for ATZ at UV285 than UV255, indicating that RNS play an important role in ATZ degradation. 3.2 Contribution of reactive species on ATZ degradation ATZ could be degraded by direct UV photolysis and reactive radicals such as HO• and RNS generated from photolysis of nitrate [9, 19]. To distinguish the respective contributions of UV photolysis, HO• and RNS on ATZ degradation in UV/nitrate system,
calculations were carried out according to the methods reported by Fang et al. [29, 30], which is shown in Table 1. There were approximately 26.0% and 86.0% of ATZ degraded by UV255/nitrate and UV285/nitrate systems, respectively, at UV fluence of 864 mJ cm-2. Direct UV photolysis (in the absence of nitrate) removed 4.0% and 12.0% of ATZ at UV255 and UV285, respectively, based on the calculated results (Figure 2A and B). As calculated, 14.5% of ATZ was removed by HO• oxidation under UV255/nitrate while only 1.0% of ATZ was removed by UV285/nitrate (Figure 2A and B).
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Correspondingly, the contribution of HO• to ATZ degradation was considerably high (55.8%) for UV255/nitrate but low (1.2%) for UV285/nitrate at UV fluence of 864 mJ cm2
(Figure 2C). On the other hand, only 28.6% of ATZ degradation was attributed to RNS
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in UV255/nitrate system while RNS contributed 84.9% to ATZ degradation in UV285/nitrate system (Figure 2C).
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Former studies also observed the formation of 2-hydroxyatrazine by direct
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photolysis of ATZ at shorter wavelengths (254-290 nm) [19, 31]. The formed 2hydroxyatrazine was too stable to be further decomposed [32], resulting in a low ATZ
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removal efficiency through UV photolysis. Photolysis of nitrate could also generate HO•, the amount of which decreased steadily with the wavelength increasing from 254
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nm to 300 nm (e.g. a quantum yield of 9% at UV254 and around 1% at UV300) [7, 9]. The calculated steady-state concentrations of HO• were 5.5 × 10-15 M and 1.2 × 10M for UV255 and UV285, respectively. Thus, the degradation of ATZ by HO• oxidation
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at UV285 was much lower than that of UV255. Still, the ATZ removal efficiency was considerably low in UV255/nitrate system compared to the sulfate radical based advanced oxidation process (AOPs) deriving from activation of sulfite [33] or peroxymonosulfate [34] and electrochemical activation of persulfate [35]. This may be due to that the reaction rate constant of ATZ with HO• (3.0 × 109 M-1s-1) is relatively
lower than that with sulfate radicals (4.2 × 109 M-1s-1). The role of RNS has shown to be important in degradation of contaminants with phenolic structure because of the presence of electron-rich moieties [3-5], while the electron-donated moieties of ATZ made it less susceptible to RNS. Interestingly, the photolyzed products of ATZ, 2-hydroxyatrazine, has electron-rich moieties which further facilitates attack by RNS. Considering the generated transformation products, higher yield of RNS in UV285/nitrate could be beneficial to the degradation of
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contaminants compared to UV255/nitrate process. Figure S3 also shows more ATZ was removed through direct UV photolysis at 285 nm than that at 255 nm. However, the contribution from UV photolysis to ATZ degradation was not significantly different
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3.3 ATZ degradation in authentic waters
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between the UV255/nitrate and UV285/nitrate processes (Figure 2A and B).
Nitrate is ubiquitous in natural waters in the range from 0.01 to 1 mM [9]. In this
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study, field water samples were collected from Lao Yinggou River (Yichang, China) on Mar 26th, May 28th, Jun 27th and Jul 19th. The nitrate concentration in this river could
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reach to 1 mM because of the overuse of fertilizer [36]. The removal efficiency of ATZ ranged from 0.7% to 12.4% for UV255 at 864 mJ cm-2 UV fluence while ATZ decreased
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by 6.3% to 44.9% for UV285 (Table S2). The results further confirmed that UV285 is
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more suitable to be used as light source in practical applications. VPA analysis was then used to distinguish the role of environmental factors (initial
concentration of nitrate, NOM, and carbonate/bicarbonate + pH) on ATZ degradation. In UV255/nitrate system, ATZ degradation was mainly dependent on the interaction between NOM and nitrate, which made the primary influence on ATZ removal (60%) (Figure 3A). The nitrate alone accounted for 13% of ATZ degradation while the
interaction between nitrate and carbonate/bicarbonate + pH achieved 12% of ATZ degradation. In UV285/nitrate system, ATZ degradation was mainly ascribed to initial nitrate concentration (64%) while the interaction between NOM and nitrate yielded 25% of ATZ degradation (Figure 3B). NOM or carbonate/bicarbonate served as scavengers of HO• [37, 38], which may affect ATZ removal in UV255/nitrate system. Interestingly, NOM and carbonate/bicarbonate were less prone to scavenge RNS [5, 39]. 3.4 Influence of environmental factors
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Influence of initial nitrate concentration. The photochemical degradation of ATZ (1 μmol) was carried out in the presence of nitrate ranging from 0.2 to 10 mM. The
removal of ATZ under UV255 increased from 15.2% to 45.8% when nitrate
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concentration was increased from 0.2 to 10 mM at 864 mJ cm-2 (Figure S5A).
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Interestingly, the conversion of ATZ under UV285 increased from 38.7% to 90.3% with nitrate concentration increasing from 0.2 mM to 10 mM (Figure S5B). The increase in
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initial nitrate concentration result in enhancement of ATZ degradation both for UV255 and UV285, which can be ascribed to the increased steady-state concentrations of HO•
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and RNS for UV255/nitrate and UV285/nitrate systems [3, 40]. Correspondingly, the kobs increased from 0.0002 cm2 mJ-1 to 0.0007 cm2 mJ-1 and from 0.0005 cm2 mJ-1 to 0.0027
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cm2 mJ-1 for UV255 and UV285, respectively (Figure 4A). Thus, the initial concentration of nitrate affected ATZ degradation in UV285/nitrate more dramatically compared to
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UV255/nitrate system, which was consistent to the VPA result. Influence of natural organic matter. The effect of NOM (0 to 10 mg-C L-1) on
ATZ degradation by nitrate photolysis was then investigated. For UV255/nitrate system, ATZ degradation was inhibited when the NOM concentration increased from 0 to 10 mg-C L-1. Higher concentration of NOM (> 1 mg-C L-1) dramatically inhibited ATZ degradation in UV255/nitrate system (Figure S6A). This is because that NOM is a good
scavenger of HO• which results in decrease in reaction between HO• and target contaminants [41, 42]. On the other hand, ATZ degradation was inhibited slightly in the UV285/nitrate system in the presence of NOM of 0-4 mg-C L-1. When NOM concentration further increased to 7 and 10 mg-C L-1, the presence of NOM even promoted the degradation of ATZ (Figure S6B). The phenomenon could be explained by the production of singlet oxygen from photolysis of NOM, irradiated by UV of higher wavelengths [43, 44], which facilitates photochemical degradation of ATZ [45].
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Thus, the interaction between NOM and photogenerated radicals from nitrate photolysis could affect ATZ degradation which is consistent with our VPA results.
Influence of initial pH. The impact of initial pH (4.0, 6.1, 7.2, 8.1 and 9.0) on ATZ
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degradation by nitrate photolysis was also studied. Results showed that ATZ degradation under UV255/nitrate was not significantly affected by solution pH (Figure
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S7A). With the initial pH increasing from 4.0 to 9.0, ATZ degradation under UV285
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increased from 59.3% (pH 4.0) to 86.0% (pH 7.2), and then decreased to 83% (pH 9.0) (Figure S7B). Previous studies about nitrate photolysis had demonstrated that acidic
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solution facilitated HOONO production (Eq. (4)), followed by the regeneration of nitrate (Eq.(10)) [28, 46], which caused the decrease in quantum yield of RNS. Thus,
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the kobs for UV285 was 0.0010 cm2 mJ-1 at pH 4.0 which was significantly lower than that at the higher pH values (Figure 4B).
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HOONO → NO3− + H+
(9)
Influence of alkalinity. The influence of bicarbonate/carbonate on ATZ
degradation by nitrate photolysis was then investigated in the range from 0 to 200 mg L-1. The inhibition of ATZ removal increased in UV/nitrate system at different wavelengths with the increase in bicarbonate/carbonate concentration (Figure S8). The phenomenon can be explained from two aspects: (1) solution pH was 7.20, 7.62, 7.93,
8.19, and 8.35 when bicarbonate concentration was 0, 50, 100, 150, and 200 mg/L, respectively, and ATZ removal was inhibited with the increase of pH; (2) the presence of carbonate/bicarbonate ions can react with HO• to produce carbonate radicals (CO3•−) as shown in the following equations [47, 48]: HCO3− + HO• → CO3•− + H2O
(10)
CO32− + HO• → CO3•− + OH−
(11)
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Thus, carbonate/bicarbonate can quench HO• and thus affect ATZ degradation in UV/nitrate system because CO3•− cannot degrade ATZ [3]. Carbonate/bicarbonate also
reacts with nitrogen species derived from nitrate photolysis in alkaline solutions as
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follows [49]:
ONOOC(O)O− → CO3•− + NO2•
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ONOO− + CO2 → ONOOC(O)O−
(12) (13)
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On consideration of the low productivity of ONOO− during nitrate photolysis, the influence of carbonate/bicarbonate on RNS was negligible [3, 9].
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3.5 Transformation products and toxicity variation of ATZ in UV285/ nitrate The role of radiation wavelength at 285 nm was then investigated for the rest of
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this study on consideration of the highest degradation efficiency of ATZ in the presence of 10 mM nitrate. The molecular weight and structures of possible transformation
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products were proposed according to the ratio of mass to charge (m/z) and retention time. Based on the products detected, the possible degradation pathways of ATZ in UV285/nitrate system are shown in Figure 5. Because of the simultaneous involvement of direct UV photolysis, HO• and RNS, different reactions (including dechlorinationhydroxylation, amine oxidation and dechlorination) take place in this system. The first route involved dechlorination-hydroxylation reactions via electron transfer. There are
two possible mechanisms for this process to produce OEIT (m/z = 198.185). One was the direct photolysis of ATZ which has been reported in previous studies [18, 19]. The other could be attributed to the reaction between ATZ and NO2• or NO• to obtain an electron and form [C8H14ClN5]•) [50] (Scheme 1). The dechlorinated-hydroxylated intermediate products (C8H15N5O) were then produced after reaction with water molecules because Cl in the above radical cation is easier to undergo nucleophilic substitution reaction compared to other moieties [3]. Then, RNS attack the C8H15N5O
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with the electron-rich moieties to form hydroxyatrazine (OAIT, Scheme 1). The second route involves attack at the side chain of ATZ. RNS, especially NO•, are likely to react
with ethylamino group or propionylamino group, which leads to subsequent generation
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of DEA (m/z = 188.069) or DIA (m/z = 174.054) with the involvement of O2-induced oxidation (Scheme 2). The third route was a dichlorination process which could be
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ascribed to cleavage of the C-Cl bond because of the direct UV photolysis of ATZ
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generating EIT and AIT [51]. Among the aforementioned products, OEIT (m/z = 198.185) has the highest intensity and its intensity increased dramatically in the initial 10 min and gradually decreased (Figure 6A). The other three compounds (DEA, DIA,
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AIT) showed similar trends with OEIT. Notably, the intensity of OAIT increased continuously with UV fluence, further suggesting the first route made the main
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contribution to ATZ degradation.
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Besides, even though the concentration of detected products decreased with the reaction time, the variation of acute toxicity of treated ATZ solution is unclear because of the potential formation of undetected products (e.g. nitrated compounds). Therefore, vibrio fischeri was used to monitor the toxicity variation during the treatment, and results were presented in Fig. S9. As shown, in the first 20 min, the acute toxicity kept decreasing, possibly due to the decreasing concentrations of ATZ and its primary
products (e.g. DEA, DIA, AIT, and OEIT). In the latter phase of ATZ degradation in UV/nitrate system (30-120 min), the acute toxicity of treated solution increased with the reaction time, indicating that further products (e.g. nitrated products) with higher toxicity were generated and accumulated in the solution. The results suggested that further ameliorations are needed for UV/nitrate system to reduce the toxicity of contaminants. 4. Conclusions
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RNS generated from nitrate photolysis have demonstrated capability of degrading
refractory contaminants under optimized operation conditions. Considering the possible application in natural water bodies, the radiation wavelength would be a key
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factor. This study demonstrated that the role of RNS in the degradation of contaminants
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with weakly electron-donating moieties (e.g. ATZ) was dependent on the radiation wavelength.
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(1) The radiation wavelength had important influence on ATZ degradation: ATZ could be removed efficiently in UV285/nitrate system (87.7% of removal efficiency at
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864 mJ cm-2 UV fluence) and inefficiently in UV255/nitrate system (35.2% of removal efficiency at 864 mJ cm-2 UV exposure).
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(2) The reactive nitrogen species made the main contribution to ATZ degradation in the
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UV285/nitrate system. The ATZ removal mainly relied on the initial concentration of nitrate according to the variance decomposition analysis.
(3) The environmental factors such as NOM, pH and carbonate/bicarbonate significantly affected the kinetics of ATZ removal in UV/nitrate system.
Declaration of interests
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Author Contribution Statement Lingjun Bu: Conceptualization; Data curation; Software; Validation; Writing - original
Ningyuan Zhu: Conceptualization; Writing - original draft. Chunquan Li: Investigation; Visualization.
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Ying Huang: Conceptualization.
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draft.
Minghao Kong: Formal analysis; Writing - review & editing.
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Xiaodi Duan: Methodology; Project administration; Supervision; Writing - review & editing.
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Dionysios D. Dionysiou: Funding acquisition; Writing - review & editing.
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Acknowledgments
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This work was supported by the National Natural Science Foundation of China (31772396). N. Zhu also acknowledgements the support from the UCAS Joint PhD Training Program. D. D. Dionysiou also acknowledges support from the University of Cincinnati through a UNESCO co-Chair Professor position on “Water Access and Sustainability” and the Herman Schneider Professorship in the College of Engineering and Applied Sciences.
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1.0
A
Ct/C0
0.8
0.6
0.4
UV255 UV285 UV365
0.2
0.0
0
20
40
60
80
100
120
Time (min) 1.0
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B
0.6
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Ct/C0
0.8
0.2
0.0
UV255 UV285
0
150
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0.4
300
450
600
750
900
-2
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UV Fluence (mJ cm )
Figure 1 A) Degradation of ATZ vs. time at different wavelengths in the presence of
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nitrate.
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nitrate; B) degradation of ATZ vs. UV fluence at UV255 and UV285 in the presence of
A 100 UV Photolysis OH. RNS
Removal (%)
80
60
40
20
0 000 0 0 0 0 200
0
400
0
600
800
UV fluence (mJ cm-2)
B 100
60
40
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Removal (%)
80
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UV Photolysis OH. RNS
0 0
200
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20
400
600
800
-2
C 100
60
RNS OH. UV Photolysis
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Contribution (%)
80
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UV fluence (mJ cm )
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40
20
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0
UV255
UV285
Figure 2 A) The removal of atrazine vs. UV fluence by direct UV photolysis, RNS and HO• at UV255/nitrate system; B) The removal of atrazine vs. UV fluence by direct UV photolysis, RNS and HO• at UV285/nitrate system; and C) The contribution (%) of direct UV photolysis, RNS and HO• on atrazine removal for UV255/nitrate and UV285/nitrate, respectively, at 864 mJ cm-2.
A
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B
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Figure 3 The variance decomposition analysis (VPA) for atrazine degradation in real water under UV255 (A) and UV285 (B).
0.0024
0.0012
UV255
UV255
D
NOM = 0 NOM = 1 mg-C L-1 NOM = 2 mg-C L-1 NOM = 4 mg-C L-1 NOM = 7 mg-C L-1 NOM = 10 mg-C L-1
0.0012
0.0006
(bi)carbonate = 0 (bi)carbonate = 50 mg L-1 (bi)carbonate = 100 mg L-1 (bi)carbonate = 150 mg L-1 (bi)carbonate = 200 mg L-1
0.0018
0.0012
0.0006
0.0000
0.0000
UV255
UV285
0.0030
0.0024
k obs(mJ-1 cm2)
kobs (mJ-1 cm2)
UV285
0.0030
0.0018
0.0012
0.0000
0.0000
0.0024
0.0018
pH = 4.0 pH = 6.1 pH = 7.2 pH = 8.1 pH = 9.0
0.0006
0.0006
C
0.0030
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0.0018
0.2 mM nitrate 2 mM nitrate 4 mM nitrate 6 mM nitrate 10 mM nitrate
UV285
-p
0.0024
k obs(mJ-1 cm2)
B
0.0030
k obs(mJ-1 cm2)
A
UV255
UV285
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Figure 4 The influence of operation parameters in ATZ removal represented by observed reaction rate constants based on UV fluence: A) the initial concentration of
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nitrate; B) the initial pH; C) the presence of NOM; and D) alkalinity.
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h
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Figure 5 Probable degradation pathways of atrazine in UV285/nitrate system.
6.0E6
A
OEIT m/z = 198.1349
Volume
4.0E6
0.0
0
20
40
60
80
100
Time (min)
4E5
140
re
3E5
2E5
DEA m/z = 188.0697 DIA m/z = 174.0541 OAIT m/z = 170.1036 AIT m/z = 154.1087
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Volume
120
-p
5E5
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2.0E6
1E5
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0
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0
20
40
60
80
100
120
140
Time (min)
Figure. 6 Evolution profiles of transformation products of ATZ in the UV285/nitrate
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process. A) OEIT and B) DEA, DIA, OAIT, and AIT.
Table 1 Data used to calculate contributions from UV photolysis, HO•, and RNS to the degradation of ATZ in the UV255/nitrate and UV285/nitrate system. [ATZ]0 = 1 µM, [nitrate]0 = 4 mM, pH = 7.2. 𝒌𝒑𝒉𝒐𝒕𝒐𝒍𝒚𝒔𝒊𝒔
Time Ct/C0 (s)
R
𝒊
𝒕𝒊
× ∫ [𝑨𝑻𝒁]𝒅𝒕
𝐤 𝐇𝐎•
photolysis
× ∫ [𝑨𝑻𝒁]𝒅𝒕
R HO•
R RNS
𝒕𝒊−𝟏
𝒕𝒊−𝟏
1.00
167
0.99
0.0005
0.0005
0.0018
0.0018
0.0036
333
0.98
0.0005
0.0010
0.0018
0.0036
0.0122
UV
1000
0.97
0.0019
0.0029
0.0071
0.0107
0.0191
255
2000
0.92
0.0029
0.0058
0.0105
0.0212
0.0494
4000
0.88
0.0055
0.0113
0.0203
0.0415
0.0700
8000
0.83
0.0103
0.0217
0.0379
0.0794
0.0720
16000
0.74
0.0178
0.0653
0.1447
0.0745
0
1.00
300
0.92
UV
600
0.84
285
1800
Jo
7200
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0.0395
0.0081
0.0006
0.0006
0.0676
0.0078
0.0160
0.0006
0.0013
0.1461
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0.0081
0.61
0.0287
0.0447
0.0023
0.0036
0.3380
0.41
0.0349
0.0796
0.0028
0.0064
0.5068
0.0407
0.1203
0.0033
0.0096
0.7300
ur
3600
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0
0.14