G Model
CCLET-6191; No. of Pages 5
X. Yang, X. Ding, L. Zhou et al.
Chinese Chemical Letters xxx (xxxx) xxx–xxx
other, depending on the target pollutants and reaction conditions.
In addition, oxygen contents in different bodies are also variable,
unlike surface environments, groundwater is often oxygen-
deficient. Therefore, for realistic applications of SR-AOPs, it is of
great importance to evaluate the impact of DO on the oxidation
efficiency and degradation pathways of target pollutants since only
few studies dealt with this point.
In our previous paper the degradation kinetic and transforma-
tion pathways of trimethoprim (TMP) were investigated systemi-
cally by thermo-activated persulfate (TAP) [11]. TMP is
a
bacteriostatic antibiotic for the treatment of infectious diseases
in humans and have been frequently detected in natural waters
[12,13]. An oxygen involved pathway was temporarily proposed by
which α-hydroxytrimethoprim (TMPꢁOH) and α-ketotrimetho-
prim (TMP=O) were generated simultaneously. However, the
detailed impacts of oxygen on degradation kinetics and mecha-
nisms still remain unclear.
Therefore, the main goal of the present study was to investigate
the impact of oxygen on TMP oxidation more deeply. Our
objectives were: 1) To evaluate the effect of oxygen on TMP
degradation kinetic; 2) to identify the oxidation products and to
record their evolution in the absence and presence of oxygen; 3) to
reveal the detailed degradation pathways and mechanisms of TMP
under different oxygen conditions.
Specifically, TAP oxidation experiments were conducted in
75 mL screw-cap cylindrical glass vials with Teflon septa at
predetermined temperature (60 ꢃC) controlled by a thermal water
bath (Xianou Instrument Manufacture Co., Ltd., Nanjing, China).
Photochemical experiments were performed using a merry-go-
round photo reactor (NaAi Instrument Manufacture Co., Ltd.,
Fig. 1. Degradation of TMP under different oxygen conditions by TAP.
([TMP]0 = 40 m
mol/L, [PS]0 = 2 mmol/L, T = 60 ꢃC, pH 7.0).
anaerobic conditions. Under control group (DO 8.23 ꢄ 0.25 mg/L),
TMPlossratewasdetectedat0.033minꢁ1,whichwasfasterthanthat
of anaerobic condition group (DO 1.52 ꢄ 0.20 mg/ L) at 0.018 min-1
(Fig. S1 in Supporting information). All the results suggested that
TMP degradation under control group was faster than that at
anaerobic condition, indicating the involvement of DO in the overall
interaction between sulfate radical and TMP.
It was widely considered sulfate radical and hydroxyl radical
was responsible for the elimination of contaminants in the TAP
ꢀ
processes [16,17]. The work of Tan et al. has reported O2 ꢁ might be
generated under the basic conditions in the antipyrine removal by
TAP [18]. Thus, spin trapping-electron paramagnetic resonance
(EPR) analysis was employed here to identify the potential
involved active species. As shown in (Fig. S2 in Supporting
information), under both two oxygen conditions, the splitting
signals with relative intensity ratio of 1:2:2:1 and a six-line signal
were observed, whose typical spectra were assigned to DMPO-ꢀOH
Shanghai, China) equipped with
a 500 W Xenon lamp and
conducted in a series of 60 mL uncapped cylindrical quartz tubes.
Appropriate volumes of TMP and PS stock solution were
transferred into the vials to achieve a total of 50 mL reaction
solution with predetermined concentrations. Anaerobic experi-
ments were carried out in an anaerobic incubator (YQI-II, CIMO,
Shanghai, China), prior to activation, the reaction solutions were
purged by N2 for 15 min to achieve a DO concentration of
1.28 ꢄ 0.25 mg/L. Reactions solutions were buffered by using
10 mmol/L phosphate, pH values remained within 7.0 ꢄ 0.1 over
the course of the experiments. Sample aliquots (0.75 mL) were
ꢀ
ꢀꢁ
and DMPO-SO4 ꢁ, respectively [19,20]. However, O2 was hardly
detected directly by EPR, possibly due to its low concentration.
These phenoꢀmꢁ ena confirmed TMP removal was mainly affected by
ꢀOH and SO4
.
To further explore the dominant species on TMP removal by
TAP processes under different oxygen conditions, the radical
scavenger experiments were conducted. The different reactivities
of tertiary butanol (TBA) and ethanol (EtOH) toward hydroxyl
radical (kꢀOH +EtOH = 2.0 ꢂ 109 L molꢁ1 s-1, kꢀOH+TBA = 5.7 ꢂ 108
L
ꢀꢁ
molꢁ1 s-1) and sulfate radical (kSO4 + EtOH = 4.65 ꢂ107 L molꢁ1 s-1,
withdrawn intermittently and quenched by 20 mL Na2S2O3
ꢀꢁ
kSO4 + TBA = 6.55 ꢂ105 L molꢁ1 s-1) could be used to distinguish the
(1 mol/L) solution to stop the reactions. Further analysis details
are illustrated in Text S1 (Supporting information). Density
functional theory (DFT) calculations were conducted in a Gaussian
09 package software [14]. Detailed calculation method was shown
in Text S2 (Supporting information). In this contribution, frontier
electron densities (FEDs) of highest occupied molecular orbital
(HOMO) and lowest unoccupied molecular orbital (LUMO) were
dominant radical species in reaction solution [21,ꢀ2ꢁ2]. In the
meanwhile, chloroform (CF) was applied to trap O2 with rate
constant of 3 ꢂ 1010 L molꢁ1 s-1 [21]. Applied in Fig. S3 (Supporting
information), without the addition of any scavenger, 85.7% TMP
removal could be achieved in the control group after 60 min. After
the addition of EtOH, TMP removal sharply decreased from 85.7%–
26.3%. When TBA replaced EtOH, the decline of TMP was
comparatively slighter. In addition, the presence ofꢀꢁCF showed
less adverse effect on TMP removal, indicating O2 playing a
minor role in the TMP oxidation. In the N2 bubbling group, same
trend was also oꢀbꢁserved similarly. All these results suggested that
overweight SO4 was the predominant oxidizing species in the
TAP process.
also calculated. Values of 2FED2
were estimated to predict
HOMO
reaction sites for electron-transfer by sulfate radicals [15].
Firstly, a comparison study was conducted to evaluate the
impact of DO on TMP oxidation by sulfate radical. The theoretical
DO concentration in an air-opened condition at 60 ꢃC was around
3.18 mg/L and this system was taken as the control group. As seen
in Fig. 1, in the case of control group, TMP underwent a fast
degradation with a rate constant of 0.042 minꢁ1. However, when
oxygen was driven out from the reaction solution (anaerobic
condition group), significant decrease on the degradation efficien-
cy was observed, with a rate constant at 0.021 minꢁ1. Correspond-
ingly, half-life time of TMP was increased from 16.5 min to
33.0 min. TMP degradation under air-saturated condition was
2-fold faster than that at anaerobic condition.
In order to obtain a deeper insight on the involved mechanism
of DO in the reaction process, oxidation products generated under
two different oxygen contents were identified by HR-MS tech-
nique. Surprisingly, no difference on the total ion chromatogram
(TIC) spectrum of TMP degradation under different conditions was
observed (Fig. S4 in Supporting information). Specifically, two
oxidation products with m/z of 307.1396 and 305.1242 (Table S1
and Fig. S5 in Supporting information) were identified as the
primary products, assigning as TMPꢁOH (lmax at 270.6 nm) and
TMP=O (lmax at 226.8, 255.0 and 293.2 nm) (Fig. S6 in Supporting
To further confirm the involvement of oxygen, TMP degradation
was also conducted in UV/PS process at ambient temperature
(20 ꢃC), by continuously bubbling N2 (0.2 L/min) to achieve
2