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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Embodiment 1
[0016] Step A: Acid analysis treatment, introducing the ink wastewater into the acid analysis tank, adjusting the pH value to 3, stirring mechanically for 30 minutes, standing for 30 minutes, separating to obtain supernatant A and precipitate A, and filtering the precipitate A, Obtain press filtrate A;
[0017] Step B: Fenton oxidation treatment, introduce the supernatant A and press filter 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 supernatant B and precipitate B, and precipitate B to press filter to obtain press filter B, the Fe 2+ and H 2 o 2 The amount 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 the press-filtrate B obtained in step B are degraded by MBR microorganisms to obtain purified water with COD<100, and the HRT is 4h during the MBR reaction treatment process.
Embodiment 2
[0020] Step A: Acid analysis treatment, introducing the ink wastewater into the acid analysis tank, adjusting the pH value to 4, stirring mechanically for 15 minutes, standing for 45 minutes, separating to obtain supernatant A and precipitate A, and filtering the precipitate A, Obtain press filtrate A;
[0021] Step B: Fenton oxidation treatment, introduce the supernatant A and press filter A obtained in step A into the Fenton oxidation tank, and add Fe 2+ and H 2 o 2 , stir, adjust the pH value, separate to obtain supernatant B and precipitate B, and precipitate B to press filter to obtain press filter B, the Fe 2+ and H 2 o 2 The amount ratio is 1:1, the stirring time is 10min, and the pH value is adjusted to 6;
[0022] Step C: MBR reaction treatment, degrade the supernatant liquid B and press-filtrate B obtained in step B through MBR microorganisms to obtain purified water with COD<100, and the HRT during the MBR reaction treatment process is 6h.
Embodiment 3
[0024] Step A: Acid analysis treatment, introducing the ink wastewater into the acid analysis tank, adjusting the pH value to 3.5, stirring mechanically for 15 minutes, standing for 40 minutes, separating to obtain supernatant A and precipitate A, and filtering the precipitate A, Obtain press filtrate A;
[0025] Step B: Fenton oxidation treatment, introduce the supernatant A and press filter A obtained in step A into the Fenton oxidation tank, and add Fe 2+ and H 2 o 2 , stir, adjust the pH value, separate to obtain supernatant B and precipitate B, and precipitate B to press filter to obtain press filter 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, degrade the supernatant liquid B and press-filtrate B obtained in step B through MBR microorganisms to obtain purified water with COD<100, and the HRT during the MBR reaction treatment process is 5h.
[0027] In the st...
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