Method for removing pentavalent antimony pollutant in water through electrochemical method
An electrochemical and pollutant technology, applied in the field of water treatment, can solve the problem of low removal rate of pentavalent antimony and achieve the effect of reducing oxidation potential
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Embodiment 1
[0027] In the electrochemical reactor, the iron plate is the anode, the copper plate is the cathode, the distance between the iron plate electrode and the copper plate cathode is 1 cm, and the ratio of the area of the plate to the volume of the water to be treated is 1 / 2 (m 2 / m 3 ). Adopt DC power supply for power supply, current density is 15A / m 2 . Formulated with Sb 3+ And Sb 5+ Of water to be treated, of which Sb 5+ And Sb 3+ The concentrations were 60μg / L and 20μg / L, and the pH of the water was adjusted to 3.5. The water to be treated is pumped into the electrochemical reactor, and the electrochemical reaction treatment time is 30 minutes. Under the above operating conditions, the Sb of the treated water 5+ And Sb 3+ The removal results are shown in Table 1. It can be seen that the antimony content in the effluent quality is lower than the limit of 5μg / L of antimony specified in my country's "Sanitary Standards for Drinking Water" (GB5749-2006).
[0028] Table 1: Electr...
Embodiment 2
[0032] In the electrochemical reactor, the iron plate is the anode, the nickel plate is the cathode, the distance between the iron plate electrode and the reduction electrode is 1.5 cm, and the ratio of the plate area to the volume of the water to be treated is 2 / 3 (m 2 / m 3 ). Adopt DC power supply for power supply, current density is 20A / m 2 . Sb in water to be treated 3+ And Sb 5+ The concentrations were 35μg / L and 12μg / L, respectively, and the pH of the water was adjusted to 5.6. Pump the water to be treated into the electrochemical reactor, and the electrochemical treatment time is 20 minutes. Under the above operating conditions, Sb in the water after treatment 5+ And Sb 3+ The removal results are shown in Table 2. It can be seen that the antimony content in the effluent quality is lower than the limit of 5μg / L of antimony specified in my country's "Sanitary Standards for Drinking Water" (GB5749-2006).
[0033] Table 2: Electrochemical treatment results of Example 2
[003...
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