Arsenic (III) oxidation and removal from artificial mine wastewater by blowing O-2 nanobubbles

This study found that with the help of O-2 nanobubble pre-oxidation treatment, effective arsenic removal was successfully achieved and is expected to be applicable on an industrial scale. The main research findings to remove arsenic are as follows. The oxidation of As(III) by blowing out O-2 nanobubbles, O-2 millimeter-sized bubbles, and air nanobubbles was studied under the condition of As(V) equilibrium at pH 1of the Pourbaix diagram. At pH 1, only O-2 nanobubbles were able to oxidize As(III) to As(V). At the same time, the oxidation rate of As(III) was about 20% in the presence of air nanobubbles and 0% in the presence of O-2 millimeter-sized bubbles. According to the extended DLVO theory, O-2 nanobubbles are unstable at acidic pH. Nanobubbles grow and break, and then center dot OH is produced. Below pH 3, H3AsO3 reacts with center dot OH and converts to H3AsO4 while As(III) is oxidized to As(V). Ferric hydroxide co-precipitation with arsenic was effective to remove arsenic ions at more than 20Fe/As mass ratio and pH higher than 4. The As(V) removal rate was higher than As(III) at acidic pH because anionic HAsO(4)(2-& nbsp;)ion could be adsorbed onto positively charged ferric hydroxide. In the artificial mine wastewater treatment, the sedimentation height of coprecipitated sludge was reduced by O-2 nanobubble utilization due to O-2 and Fe(OH)(3) hetero-coagulation.