Method for quickly removing pentavalent antimony pollutant in water by combining sodium sulfite and electrochemistry
A sodium sulfite, electrochemical technology, applied in the field of water treatment, to achieve the effect of reducing the residual concentration and optimizing the removal effect
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Embodiment 1
[0021] In the electrochemical reactor, the iron plate is the anode, the steel plate is the cathode, the distance between the iron plate anode and the steel plate cathode is 1 cm, and the ratio of the area of the plate to the volume of water to be treated is 1 / 10 (m 2 / m 3 ). Powered by DC power supply, the current density is 1mA / cm 2 . Formulated with Sb 5+ of water to be treated, where Sb 5+ The concentration is 60μg / L, adjust the pH value of water to 4.5, and add sodium sulfite solution with a total concentration of 1.0mmol / L in the electrochemical reactor. The water to be treated is pumped into the electrochemical reactor, and the reaction treatment time is 20 minutes. Under the above operating conditions, the content of antimony in the treated effluent is 2.3 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, without adding sodium s...
Embodiment 2
[0023] In the electrochemical reactor, the iron plate is the anode, the copper plate is the cathode, the distance between the iron plate anode and the copper plate cathode is 1.5 cm, and the ratio of the area of the plate to the volume of water to be treated is 1 / 5 (m 2 / m 3 ). DC power supply is used for power supply, and the current density is 5A / m 2 . Sb in water to be treated 5+ The concentration is 35μg / L, the pH value of the water is adjusted to 5.6, and the sodium sulfite solution with a total concentration of 0.5mmol / L is added to the electrochemical reactor. The water to be treated is pumped into the electrochemical reactor, and the electrochemical treatment time is 15 minutes. Under the above operating conditions, the concentration of antimony in the treated water is 2 μg / L. Under the above operating conditions, no sodium sulfite solution was added, and the antimony concentration in the treated water was 6 μg / L.
Embodiment 3
[0025] In the electrochemical reactor, the iron plate is the anode, the copper plate is the cathode, the distance between the iron plate anode and the copper plate cathode is 1.5 cm, and the ratio of the area of the plate to the volume of water to be treated is 1 / 5 (m 2 / m 3 ). DC power supply is used for power supply, and the current density is 1A / m 2 . Sb in water to be treated 5+ The concentration is 15μg / L, and the sodium sulfite solution with a total concentration of 0.05mmol / L is added to the electrochemical reactor to adjust the pH value of the water to 6.5. The water to be treated is pumped into the electrochemical reactor, and the electrochemical treatment time is 5 minutes. Under the above operating conditions, the concentration of antimony in the treated effluent was 0.9 μg / L. Under the above operating conditions, no sodium sulfite solution was added, and the concentration of antimony in the treated water was 3.2 μg / L.
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