Treatment method of dairy product wastewater
A dairy product wastewater and treatment method technology, applied in the field of dairy product wastewater treatment, can solve the problems of secondary pollution, increased treatment costs, inability to completely degrade protein and fat, etc., achieve less residual sludge, low energy consumption, and reduce secondary pollution. Effects of Secondary Pollution and Treatment Costs
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Embodiment 1
[0034] The milk powder configuration simulated dairy wastewater is used as the treatment object, and its COD concentration is 3000mg / L, and the total nitrogen concentration is 70mg / L. First flow it into the isoelectric point sedimentation tank 1 to remove casein, part of whey protein and fat. After this step, it is measured that the COD concentration of the wastewater is reduced to 2100-2300 mg / L, and the total nitrogen concentration is reduced to 13-17 mg / L. Then it flows into the filter tank 2, and after filtering the suspended solids, the waste water enters the two-stage anaerobic fermentation reaction tank 3. The wastewater first enters the hydrogen-producing anaerobic fermentation reaction tank 31, and the residence time of the wastewater is 12 hours. The COD concentration drops to 1700-2100 mg / L, and the total nitrogen concentration drops to 11-16 mg / L. Then the wastewater enters the methane-producing anaerobic fermentation reaction tank 32, the residence time of the was...
Embodiment 2
[0036] Taking the actual dairy wastewater as the treatment object, its COD concentration is 1800mg / L and the total nitrogen concentration is 50mg / L. Firstly, the waste water is passed into the isoelectric point sedimentation tank 1 to remove casein, some whey protein and fat, and the COD concentration of the waste water is reduced to 1200-1400 mg / L, and the total nitrogen concentration is reduced to 10-13 mg / L. The waste water then flows into the filter tank 2, and after filtering the suspended solids, the waste water enters the two-stage anaerobic fermentation reaction tank 3. The waste water first enters the hydrogen-producing anaerobic fermentation reaction tank 31 , the residence time of the waste water is 12 hours, the COD concentration drops to 1000-1200 mg / L, and the total nitrogen concentration drops to 9-12 mg / L. The waste water enters the methane-producing anaerobic fermentation reaction tank 32, and its residence time is 24 hours, the COD concentration further drops...
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