Biological treatment method and apparatus for organic wastewater
A biological treatment and organic technology, applied in the direction of biological treatment equipment, biological sludge treatment, sustainable biological treatment, etc., can solve the problem of not being able to use multi-stage activated sludge method
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Embodiment 1
[0065] Such as image 3 As shown, the first biological treatment tank (activated sludge tank (no sludge return)) 1A with a capacity of 3.6 L, the second biological treatment tank (activated sludge tank) 1B with a capacity of 15 L, the sedimentation tank 2, An experimental device connected to a sludge treatment tank 3 with a capacity of 3 L was used to treat the organic waste water of the present invention. A immersion membrane 4 with a pore diameter of 10 μm was installed in the sludge treatment tank 3 . The pH of the first biological treatment tank 1A and the second biological treatment tank 1B was adjusted to 6.8, and the pH of the sludge treatment tank 3 was adjusted to 5.0. The sludge in the separated sludge of the settling tank 2 was sent to the sludge treatment tank 3 at 0.5 L / d, and the other sludge was returned to the second biological treatment tank 1B. The excess sludge was extracted from the sludge treatment tank 3 at 0.2 L / d, and the permeate passing through the ...
Embodiment 2
[0068] Such as figure 1 As shown, the organic wastewater treatment of the present invention is carried out using an experimental device that connects a biological treatment tank (activated sludge tank) 1 with a capacity of 15 L, a sedimentation tank 2, and a sludge treatment tank 3 with a capacity of 3 L. . A immersion membrane 4 with a pore diameter of 10 μm was installed in the sludge treatment tank 3 . The pH of the biological treatment tank 1 was adjusted to 6.8, and the pH of the sludge treatment tank 3 was adjusted to 5.0. The sludge in the separated sludge of the sedimentation tank 2 was sent to the sludge treatment tank 3 at 0.5 L / d, and the other sludge was returned to the biological treatment tank 1 . The excess sludge was extracted from the sludge treatment tank 3 at a rate of 0.36 L / d, and the permeate passing through the immersion membrane 4 was sent to the biological treatment tank 1 at a rate of 0.14 L / d. In this sludge treatment tank 3, lecithin was added on...
Embodiment 3
[0071] Except in Example 1, a part of the treatment liquid of the first biological treatment tank 1A was concentrated by centrifugation at a speed of 12000 rpm for 5 minutes, and the concentrate was added to the sludge treatment tank 3 at 105 mg-COD / d ( The ratio of 5% of the COD of the separated sludge) is added in the sludge treatment tank 3 (and, the diluent generated by concentration is sent to the second biological treatment tank 1B.), in addition, under the same conditions Under the treatment, the sludge conversion rate was 0.08kg-MLSS / kg-BOD. The BOD of the treated water (the supernatant from the precipitation tank 2) was below the detection limit.
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