1 Introduction
Bromate () is classified as a Group 2B substance (possibly carcinogenic to humans) by the International Agency for Research on Cancer. The maximum contaminant level for ion in drinking water is set in China as 10 μg/L [1], which is the provisional guideline value recommended by the World Health Organization [2]. is generated by oxidation of bromide in water through disinfection processes such as ozonation processes [3], TiO2 photo-catalysis [4], and processes [5], and so on. In particular, during the ozonation of drinking water, the formation of becomes a problem for bromide levels of 50 μg/L–100 μg/L [6]. Therefore, it is desirable to develop effective techniques to control , especially when the Br level is high in the source water, for instance, in regions with saltwater intrusion.
A number of methods were investigated to minimize generation during ozonation or to remove excessive . Although pH suppression, ammonia addition and chlorine-ammonia addition are applicable in ozone sterilization plants [3, 6, 7], they are not suitable for source waters with high level of ammonia or alkalinity due to potential side effects [8, 9]. Also, it is difficult to remove formed during ozonzation, especially for low levels. is non-biodegradable and highly stable in water. Up to now, technologies for removal include activated carbon adsorption [10], photo-catalytic degradation [11], ion exchange [12], electrochemical reduction [13], etc. The methods may achieve high removal efficiency of under certain conditions. For example, at concentrations of 50, 100 or 200 μg/L, the removal efficiency can be over 90% by employing an anion-exchange membrane [12]. However, the approaches are still in the laboratory evaluation and development stages.
Irradiation with gamma-rays or electron beam is as a promising and clean approach for environmental protection. Pilot-scale and industrial-scale studies have shown that the ionizing radiations are effective in decomposing toxic and refractory pollutants, and in disinfecting pathogenic micro-organisms in drinking water, wastewater, and waste sludge [14, 15]. Radiation technology is advantageous in that it does not use any chemical compounds (this is often, cost-effective), hence the attractiveness in treatment of drinking water. While other advanced oxidation processes (AOPs) are based on oxidation of toxic substances just by hydroxyl radicals (⋅OH) and/or other oxidants, ionizing radiations generate simultaneously ⋅OH and highly reducing species such as ⋅eaq-, which play an important role in degrading pollutants [16]. Zhou et al. [17] revealed that when bromide-containing water was irradiated by gamma rays, could be formed only in N2O saturated solutions when was converted into ⋅OH. Inspired by this result and considering that the Br is in its higher oxidation state in , we carried out this study to investigate the reductive removal of in water by 60Co γ-rays, and to determine the effect of various experimental factors on the efficiency of the removal of bromate.
3 Results and Discussion
3.1 Effect of dose and initial concentration
Air-equilibrated solutions with initial concentrations of 30 μg/L–210 μg/L and with dissolved oxygen of about 8 mg/L were irradiated to 1 kGy–10 kGy. The removal rates of are illustrated in Fig. 1(a) and percentage of bromine recovery (considering only and Br- in the reaction systems) is shown in Fig. 1(b).
From Fig. 1, was degraded effectively by gamma-rays. The removal rate of increased with the dose and decreased with increasing initial concentrations. At 30.7 μg/L and 4.0 kGy, 73% was decomposed and the residual was 8.3 μg/L, which is below the maximum contaminant level of 10 μg/L. Figure 1 shows that at a given dose, the recovery increased with the initial concentration, but the removal rates did not change significantly. At higher levels, there were less recombination of reactive radicals (such as , ·OH+·OH → H2O2, etc.) with more radicals reacting with . However, the formation of intermediate compounds, and the oxidation of Br- and the intermediates by ⋅OH radicals, made the reaction system complicated [17-19]. It was reported that bromide could be oxidized to when ⋅OH radicals acted as the only oxidant and that HOBr/OBr- are the requisite intermediates [18]. may exist in our reaction systems because of the oxidation of HOBr/OBr- by ⋅OH radicals [3]. In Fig. 1(b), at 30.7 and 86.2 μg/L of , the Br recovery decreased at first and then increased with the dose, indicating that the amount of bromine intermediates would agree with the opposite tendency. On the other hand, Zhou et al. [17] and LaVerne et al. [19] reported that Br- could not be oxidized to by irradiating air-equilibrated NaBr solutions due to recycling of the oxidized species of bromine element by , ⋅H and/or , which implies that the reduction of and bromine intermediates is inevitable under similar operation condition. Therefore, we can infer that the amount of intermediates at 165 and 210 μg/L follows a similar tendency to that at 30.7 and 86.2 μg/L , and that all the and the intermediates are reduced to Br- at sufficiently higher absorbed doses.
3.2 Effect of saturated atmosphere
In order to explore the atmosphere effect, aqueous solutions with high level and saturated with air, N2, O2 or N2O were irradiated to 1 kGy–10 kGy. As shown in Fig. 2, for the solution degassed by N2, the removal rate of was near 98% and its concentration reduced remarkably to 7.6 μg/L at 4.0 kGy. At a given irradiation dose, the removal efficiency of decreased in the order of N2, air, O2, and N2O.
The general reaction of radiolysis of N2-saturated water can be written as Eq. (1) [20, 21], where the numbers are G-values, which are defined as the number of formed or decomposed molecules per 100 eV absorbed energy.
(1)
As a powerful reducing agent with a standard reduction potential of -2.9 V, hydrated electron () react quickly with , as shown in Eq. (2), while ⋅H reacts in a much slow rate with , as shown in Eq. (3) [21].
(2)
(3)
The reactions of ⋅H and with O2 produce HO2. and . as shown in Eqs. (4) and (5), respectively [20], which also reduce possibly via Eqs. (6) and (7). However, according to Fig. 2, it is reasonable to infer that the reduction of by is slower than that by .
(4)
(5)
(6)
(7)
On the other hand, the concentration decreased just slightly and no Br- ion was detected in the N2O-saturated solutions, when and ⋅H generated through Eq. (1) were effectively converted into ⋅OH radicals by N2O, as shown in Eqs. (8) and (9) [21]. It was reported that could react with ⋅OH radical and form radical, which was further dissociated to BrO. radical, as shown in Eqs. (10) and (11) [22]. However, BrO- radicals could be disproportionate to and HOBr/OBr- and then reform through oxidation by ⋅OH radicals. As a result, the variation of the concentration was small in the N2O-saturated solutions (Fig. 2).
(8)
(9)
(10)
(11)
3.3 Effect of pH
To further elucidate efficiency of different reactive radicals in reducing , air- and N2-saturated solutions of different pH values were irradiated. Figure 3 shows the results. The pH increase had a positive impact on removal in the N2-saturated conditions, with the removal rate being 88% at pH 11 and only 28% at pH 3.3. By radiolysis of N2-saturated water, the concentrations of ⋅H and radicals generated varied with the pH value, with more but less ⋅H formed under high pH conditions [20]. The amount of was negligible at pH 3.3 and ⋅H almost disappeared at pH 11, while the generation of ⋅OH radicals remains nearly constant in the pH range studied [20]. Therefore, from Fig. 3, is much more effective than ⋅H in reducing , and is the main reactive radical account for the removal of .
On the other hand, the removal rate of in air-saturated solutions was lower and it increased a bit with the pH value. According to Eqs. (1), (4) and (5), the main reactive species formed under these conditions were and ⋅OH, with more radicals, and less radicals formed at high pH values, but amount of ⋅OH radicals was nearly constant. Therefore, it can be sure that radicals are less powerful than HO2. radicals in reducing . Based on the results of Figs. 2 and 3, the efficiency of decomposing by reactive species was in the order of .
3.4 Effect of coexisting anions
The presence of coexisting anions in water is known to affect the radiolytic degradation of pollutants [21]. The effects of 1 mmol/L Cl-, , or anions on the radiolytic degradation of solutions are shown in Fig. 4(a). For N2O-saturated solutions, they had little effect on degradation of , as they could neither compete with N2O for reacting with or ⋅H, nor act as effective scavengers of the main existing radical (namely, ⋅OH). For similar reason, the addition of Cl- or anions showed little influence, too, on removal under or air-saturated conditions.
The effects of anions on removal are more complex. On one hand, anions react with ⋅OH and play a role as ⋅OH scavenger, as shown in Eqs. (12) and (13) [21], hence the indirect promotion of removal [17, 19] . On the other hand, the formed active carbonate radicals () through Eqs. (12) and (13) can oxidize the intermediates of bromine and form precursors again, as shown in Eqs. (14) and (15) [23] . In Fig. 4(a), adding slightly increased the removal of .
(12)
(13)
(14)
(15)
However, it was observed that the presence of anion suppressed significantly the reduction in both N2-- and air-saturated solutions. According to Fig. 4(a), the removal rate of decreased from 74.7% to 10.9% by adding 1 mmol/L in the N2-saturated atmosphere. By adding 1 to 10 mg/L nitrate (measured on basis of nitrogen content), the results of removal under N2-, O2- or air-saturated conditions, are shown in Fig. 4(b). In all the three atmospheres, there existed an inhibition effect, which was enhanced with increasing concentrations of . For example, in air-saturated solutions, the removal rate decreased more than a half when 10 mg/L was added (the drinking water standard of nitrate in China is 10 mg/L). The reason of inhibition can be attributed to the scavenging of by ions, as shown in Eq. (16),
(16)
and the reaction rate is very fast according to Ref. [21]. From Fig. 4, we know that the product of and , namely , and its further decay products, are incapable or ineffective in decomposing . As a result, the efficiency of removal is reduced, so the operation cost shall be carefully considered in irradiation removal of from water of high nitrate levels.
4 Conclusion
Bromate removal by γ-irradiations process was investigated, on influence factors of the absorbed dose, initial concentration, gas saturation, pH value, and coexisting anions in aqueous solution. The main results are as follows:
(1) Gamma-irradiations are efficient in removing at neutral conditions in air-saturated atmosphere (normal condition of drinking water).
(2) The efficiency of removal decreased in the order of N2 >> air > O2 > N2O atmosphere at a given dose, and higher pH value was beneficial for removal.
(3) was removed by reactive species such as , ⋅H, HO2. and , following by the order of , and played the main role in decomposing.
(4) Coexisting anions (Cl-, and ) exerted little effect on removal. However, can significantly suppress removal due to the scavenging of by .