A treatment method for simultaneously removing multiple metal ions in manganese-containing wastewater
A treatment method, metal ion technology, applied in the field of water treatment, can solve the problems of shortening hydraulic retention time, increasing process complexity, increasing treatment cost, etc., and achieves the effects of saving chemical dosage, reducing specific surface area, and reducing treatment cost
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Embodiment 1
[0032] This embodiment selects polluted high-manganese-containing water from a mining area in Guangxi. The calcium ion concentration in the raw water is 324.5mg / L, the magnesium ion concentration is 53.9mg / L, and the pH is 6.89. Other water quality parameters are shown in Table 1. The invented manganese removal process removes manganese, and the treatment temperature is 14°C.
[0033] S1. Add 24.29mg / L potassium permanganate to the raw water and adjust the pH to 8.0 (theoretically, when the molar ratio of potassium permanganate to manganese ions is 2:3, the manganese ions can be completely oxidized into insoluble Manganese dioxide, that is, 1 mg manganese theoretically requires 1.92 mg potassium permanganate. The concentration of manganese ions in raw water is 15.1 mg / L, and theoretically 28.99 mg / L of potassium permanganate is required to completely oxidize divalent manganese ions into di Manganese oxide), while oxidizing for 2min at a stirring speed of 300r / min to carry out ...
Embodiment 2
[0040] The steps described in embodiment 2 are as follows:
[0041] S1. Add 24.29mg / L potassium permanganate to the raw water and adjust the pH to 7.5 (theoretically, when the molar ratio of potassium permanganate to manganese ions is 2:3, the manganese ions can be completely oxidized into insoluble Manganese dioxide, that is, 1 mg manganese theoretically requires 1.92 mg potassium permanganate. The concentration of manganese ions in raw water is 15.1 mg / L, and theoretically 28.99 mg / L of potassium permanganate is required to completely oxidize divalent manganese ions into di Manganese oxide), while oxidizing for 2min at a stirring speed of 300r / min to carry out pre-oxidation;
[0042] S2. After the pre-oxidation is finished, add 35.19mg / L polyaluminum chloride and stir rapidly at 300r / min for 15min;
[0043] S3. Stir at a medium speed of 50r / min for 2min;
[0044] S4. Stir at a slow speed of 20r / min for 5min for flocculation;
[0045] S5. Measure the turbidity of the super...
Embodiment 3
[0047] Repeat Example 2 with the same steps described above, the difference is that 40.39 mg / L of polyferric sulfate is added in the step S2.
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