Method for treating ink wastewater
A technology of ink wastewater and treatment method, which is applied in the field of environmental protection, can solve the problems of poor treatment effect of refractory macromolecular organic matter, unstable effluent water quality, etc., and achieve good effect, stable effluent water quality, and high COD effect
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[0015] Example 1
[0016] Step A: Acid precipitation treatment, introduce the ink wastewater into the acid precipitation tank, adjust the pH value to 3, mechanically stir for 30 minutes, and stand for 30 minutes, and then separate to obtain the supernatant A and the precipitate A. The precipitate A is filtered by pressure. Obtain press filtrate A;
[0017] Step B: Fenton oxidation treatment, introduce the supernatant A and press filtrate A obtained in step A into the Fenton oxidation tank, and add Fe2+ and H 2 O 2 , Stir, adjust the PH value, separate to obtain the supernatant B and the precipitate B, press the precipitate B to obtain the filtrate B, the Fe 2+ And H 2 O 2 The ratio is 1:10, the stirring time is 20min, and the pH value is adjusted to 8;
[0018] Step C: MBR reaction treatment, the supernatant B and press filtrate B obtained in step B are degraded by MBR microorganisms to obtain COD For purified water <100, HRT is 4h during MBR reaction treatment.
Example Embodiment
[0019] Example 2
[0020] Step A: Acid precipitation treatment, introduce the ink waste water into the acid precipitation tank, adjust the pH value to 4, mechanically stir for 15 minutes, stand for 45 minutes, separate to obtain supernatant A and sediment A, and filter the sediment A. Obtain press filtrate A;
[0021] Step B: Fenton oxidation treatment, the supernatant A and press filtrate A obtained in step A are introduced into the Fenton oxidation tank, and Fe is added 2+ And H 2 O 2 , Stir, adjust the PH value, separate to obtain the supernatant B and the precipitate B, press the precipitate B to obtain the filtrate B, the Fe 2+ And H 2 O 2 The amount ratio is 1:1, the stirring time is 10 minutes, and the pH value is adjusted to 6;
[0022] Step C: MBR reaction treatment, the supernatant B and press filtrate B obtained in step B are degraded by MBR microorganisms to obtain COD For purified water <100, HRT is 6h during MBR reaction treatment.
Example Embodiment
[0023] Example 3
[0024] Step A: acid precipitation treatment, introduce the ink waste water into the acid precipitation tank, adjust the pH value to 3.5, mechanically stir for 15 minutes, and stand for 40 minutes, and then separate to obtain supernatant A and sediment A. The sediment A is filtered by pressure. Obtain press filtrate A;
[0025] Step B: Fenton oxidation treatment, the supernatant A and press filtrate A obtained in step A are introduced into the Fenton oxidation tank, and Fe is added 2+ And H 2 O 2 , Stir, adjust the PH value, separate to obtain the supernatant B and the precipitate B, press the precipitate B to obtain the filtrate B, the Fe 2+ And H 2 O 2 The amount ratio is 1:6, the stirring time is 15min, and the pH value is adjusted to 8;
[0026] Step C: MBR reaction treatment, the supernatant B and press filtrate B obtained in step B are degraded by MBR microorganisms to obtain COD For purified water <100, HRT is 5h during MBR reaction treatment.
[0027] In the ...
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