PVA-containing desizing wastewater treatment method
A technology for desizing wastewater and treatment method, which is applied in textile industry wastewater treatment, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problems of wastewater treatment impact, low BOD removal rate, etc. Cleaning treatment, COD and BOD removal rates are not high and efficient, and the effect of improving the treatment effect
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Embodiment 1
[0030] A PVA-containing desizing wastewater treatment method, comprising the following steps:
[0031] S1. The desizing wastewater containing PVA enters the first-stage sewage coagulator, and PAC and / or decolorizing agent are added to the first-stage sewage coagulator for coagulation; The dosage of dosage is 500mg / L. The flocculation sedimentation enters the sludge thickening tank, and the supernatant enters the intermediate tank.
[0032] S2. The effluent from the first-stage sewage coagulator enters the Fenton oxidation system through the lift pump for oxidation; in the Fenton oxidation tower, H 2 O 2 The total dosage is 100mmol / L, the pH is controlled to 3.5, the amount of iron filings is 10g / L, the reaction time is 30min, the effluent PVA concentration is 0.94mg / L, the removal rate is 97%, the COD removal rate is 22.3%, BOD / COD From 0.12 of the original technology to 0.29, the biodegradability is improved.
[0033] S3. The effluent from the Fenton oxidation system ente...
Embodiment 2
[0037] A PVA-containing desizing wastewater treatment method, comprising the following steps:
[0038] S1. The desizing wastewater containing PVA enters the first-stage sewage coagulator, and PAC and / or decolorizing agent are added to the first-stage sewage coagulator for coagulation; The dosage of dosage is 500mg / L. The flocculation sedimentation enters the sludge thickening tank, and the supernatant enters the intermediate tank.
[0039] S2. The effluent from the first-stage sewage coagulator enters the Fenton oxidation system through the lift pump for oxidation; in the Fenton oxidation tower, H 2 O 2 The total dosage is 150mmol / L, the pH is controlled at 4, the amount of iron filings is 15g / L, the reaction time is 30min, the effluent PVA concentration is 0.9mg / L, the removal rate is 99%, the COD removal rate is 23.6%, BOD / COD From 0.12 of the original technology to 0.34, the biodegradability is improved.
[0040] S3. The effluent from the Fenton oxidation system enters ...
Embodiment 3
[0044] A PVA-containing desizing wastewater treatment method, comprising the following steps:
[0045] S1. The desizing wastewater containing PVA enters the first-stage sewage coagulator, and PAC and / or decolorizing agent are added to the first-stage sewage coagulator for coagulation; The dosage of the dosage is 800mg / L. The flocculation sedimentation enters the sludge thickening tank, and the supernatant enters the intermediate tank.
[0046] S2. The effluent from the first-stage sewage coagulator enters the Fenton oxidation system through the lift pump for oxidation; in the Fenton oxidation tower, H 2 O 2 The total dosage was 200mmol / L, the pH was controlled at 4, the amount of iron filings was 15g / L, the reaction time was 30min, the effluent PVA concentration was 0.89mg / L, the removal rate was 99.2%, the COD removal rate was 24.1%, and the BOD / COD From 0.12 of the original technology to 0.35, the biodegradability is improved.
[0047] S3. The effluent from the Fenton ox...
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