Complex coagulant for advanced treatment of biochemical tail water, and its preparation method and application
A technology of advanced treatment and coagulant, which is applied in the direction of flocculation/sedimentation water/sewage treatment, etc., to achieve the effect of facilitating reuse, strong stability, and dense flocs
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Embodiment 1
[0023] In Example 1 of the present invention, using bentonite, scrap iron filings, and boron mud to prepare boron-containing polysilicon-aluminum-iron, the specific steps are as follows:
[0024] (1) Alkaline hydrolysis under heating: Mix 4mol / L caustic soda solution and bentonite to react with each other.
[0025] The solid ratio is 3:1, the temperature is 150°C, and the reaction time is 4 hours. The supernatant is collected to adjust the pH to 7, and the alkaline hydrolyzed substance is obtained after aging for 90 minutes.
[0026] (2) Acid leaching under heating: add pyrite slag, 5mol / L waste sulfuric acid and hydrogen peroxide to the residue of step 1, mix and stir to react, the liquid-solid ratio of the waste sulfuric acid solution to the residue of step 1, and pyrite slag The ratio is 3:1, the temperature is 100°C, and the reaction time is 4h. The supernatant liquid collected is the acid leaching material.
[0027] (3) Slow concentration and polymerization: slowly add the acid l...
Embodiment 2
[0029] In Example 2 of the present invention, kaolin, iron scraps, and boron mud are used to prepare boron-containing polysilico-aluminum-iron, and the specific steps are as follows:
[0030] (1) Alkaline hydrolysis under heating: Mix 6mol / L of caustic soda solution and kaolin to react with each other.
[0031] The solid ratio is 6:1, the temperature is 180°C, and the reaction time is 6h. The supernatant is collected to adjust the pH to 6, and the alkaline hydrolyzed substance is obtained after aging for 180min.
[0032] (2) Acid leaching under heating: Add scrap iron filings, 6mol / L waste sulfuric acid and sodium hypochlorite to the residue in step 1, and mix and stir to react. The liquid-to-solid ratio of the waste sulfuric acid solution to the residue and scrap iron filings in step 1 is 6 :1, the temperature is 150℃, the reaction time is 6h, the supernatant liquid collected is the acid leaching material.
[0033] (3) Slow concentration polymerization: slowly add the acid leaching m...
Embodiment 3
[0035] (1) Alkaline hydrolysis under heating: Mix 5mol / L caustic soda solution and gibbsite for reaction. The liquid-to-solid ratio of caustic soda solution and gibbsite is 5:1, the temperature is 200℃, and the reaction time is 8h. Adjust the pH value of the clear liquid to 6, and obtain the alkaline hydrolyzed substance after aging for 360 minutes.
[0036] (2) Acid leaching under heating: Add pyrite slag, 5mol / L waste sulfuric acid and catalytic oxidant to the residue of step 1, and mix and stir to react. The waste sulfuric acid solution is mixed with the residue of step 1, and the liquid-solid solution of pyrite slag The ratio is 4:1, the temperature is 130°C, and the reaction time is 8 hours. The supernatant liquid collected is the acid leaching material.
[0037] (3) Slow concentration polymerization: slowly add the acid leaching material, boron sludge, to the alkali hydrolyzed material, and quickly stir the polymerization reaction for 60 minutes. The volume ratio of the acid ...
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