Method for removing pentavalent antimony pollutants in water through manganese ion enhanced electrochemistry
A manganese ion and electrochemical technology, applied in the field of manganese ion-enhanced electrochemical removal of pentavalent antimony pollutants in water, can solve problems such as inapplicability
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Embodiment 1
[0018] In an electrochemical reactor, the iron plate is the anode and the steel plate is the cathode. Powered by DC power supply, the current density is 10mA / cm 2 , the plate area and the volume of water to be treated are 1 / 10m 2 / m 3 , the plate spacing is 1cm. Formulated with Sb 5+ of water to be treated, where Sb 5+ Concentration is 500mg / L, adjust the pH value of water to 5.5, pump the water to be treated into the electrochemical reactor, then add manganese sulfate solution, so that the final concentration of the manganese sulfate solution in the electrochemical reactor is 5.0 mmol / L. The reaction treatment time was 20 minutes. Under the above operating conditions, the content of antimony in the treated effluent is 2.5 μg / L, which is lower than the limit concentration of antimony 5 μg / L stipulated in my country’s “Drinking Water Sanitation Standard” (GB5749-2006). Under the above operating conditions, manganese sulfate solution is not added, and the concentration of...
Embodiment 2
[0020] In an electrochemical reactor, the iron plate is the anode and the steel plate is the cathode. DC power supply is used for power supply, and the current density is 0.5A / m 2 , the plate area and the volume of water to be treated are 1 / 10m 2 / m 3 , the plate spacing is 1cm. The water to be treated is pumped into the electrochemical reactor, and the Sb in the water to be treated 5+ The concentration was 250 μg / L, the pH value of the water was adjusted to 6.5, and manganese chloride solution was added so that the final concentration of the manganese chloride solution in the electrochemical reactor was 0.5 mmol / L. The electrochemical treatment time was 15 minutes. Under the above operating conditions, the concentration of antimony in the treated water is 3.5 μg / L. Under the above operating conditions, no manganese chloride solution was added, and the concentration of antimony in the treated water was 18 μg / L.
Embodiment 3
[0022] In an electrochemical reactor, the iron plate is the anode and the steel plate is the cathode. DC power supply is used for power supply, and the current density is 7A / m 2 , the plate area and the volume of water to be treated are 1 / 5m 2 / m 3 , The distance between the plates is 2cm. Pump the water to be treated into the electrochemical reactor, the Sb in the water to be treated 5+ The concentration was 50 mg / L, the pH value of the water was adjusted to 4, and manganese sulfate solution was added so that the final concentration of the manganese sulfate solution in the electrochemical reactor was 2.0 mmol / L. The electrochemical treatment time was 5 minutes. Under the above operating conditions, the concentration of antimony in the treated effluent was 1.5 μg / L. Under the above operating conditions, manganese sulfate solution is not added, and the concentration of antimony in the treated water is 35 μg / L.
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