Bromate (BrO 3 − ) in drinking water is traditionally seen as an ozonation byproduct from the oxidation of bromide (Br − ), and its formation during chlorination is usually not significant. This study shows enhanced bromate formation during chlorination of bromide-containing waters in the presence of cupric oxide (CuO). CuO was effective to catalyze hypochlorous acid (HOCl) or hypobromous acid (HOBr) decay (e.g., at least 10 4 times enhancement for HOBr at pH 8.6 by 0.2 g L −1 CuO). Significant halate concentrations were formed from a CuO-catalyzed hypohalite disproportionation pathway. For example, the chlorate concentration was 2.7 ± 0.2 μM (225.5 ± 16.7 μg L −1 ) after 90 min for HOCl (C o = 37 μM, 2.6 mg L −1 Cl 2 ) in the presence of 0.2 g L −1 CuO at pH 7.6, and the bromate concentration was 6.6 ± 0.5 μM (844.8 ± 64 μg L −1 ) after 180 min for HOBr (C o = 35 μM) in the presence of 0.2 g L −1 CuO at pH 8.6. The maximum halate formation was at pHs 7.6 and 8.6 for HOCl or HOBr, respectively, which are close to their corresponding pK a values. In a HOCl−Br − −CuO system, BrO 3 − formation increases with increasing CuO doses and initial HOCl and Br − concentrations. A molar conversion (Br − to BrO 3 − ) of up to (90 ± 1)% could be achieved in the HOCl−Br − −CuO system because of recycling of Br − to HOBr by HOCl, whereas the maximum BrO 3 − yield in HOBr−CuO is only 26%. Bromate formation is initiated by the formation of a complex between CuO and HOBr/ OBr − , which then reacts with HOBr to generate bromite. Bromite is further oxidized to BrO 3 − by a second CuO-catalyzed process. These novel findings may have implications for bromate formation during chlorination of bromide-containing drinking waters in copper pipes.
■ INTRODUCTIONThe formation of bromate during the ozonation of bromidecontaining waters has been intensively studied. 1−5 In the presence of ozone, bromate is produced from the reactions of ozone and ·OH radicals with bromide (Br − ), via several intermediates including hypobromite (BrO − ) and bromite (BrO 2 − ). 5 Because bromate is potentially carcinogenic, it is regulated in potable water at a maximum contaminant level (MCL) of 10 μg L −1 in many countries. 6−8 Moreover, bromate is stable, and there is currently no economically feasible technology to remove it once it is formed. 9 Therefore, the treatment conditions have to be optimized in some cases to mitigate bromate formation while disinfection is still guaranteed (e.g., ammonia addition and lowering the pH 9 ).