Method for reinforcing adsorption-biodegradation (AB) denitrification technology by use of heterotrophic nitrification-aerobic denitrification bacteria
A technology of aerobic denitrification and heterotrophic nitrification, which is applied in the field of biologically enhanced denitrification by AB process, can solve the problems of not being able to meet the discharge requirements and lack of efficient denitrification, so as to increase the daily treatment capacity, ensure the target of denitrification, and reduce sludge The effect of performance improvement
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Embodiment 1
[0031] In this embodiment, the method of the present invention and the ordinary AB sewage treatment method are used as a comparative experiment. Reaction device 1 is an AB process reaction device enhanced with PCN series microorganisms, and reaction device 2 is a common AB process reaction device.
[0032] All reactors of AB process are made of organic glass, see image 3 As shown, the designed treatment water volume is 50L / d, the effective volume of the aeration tank in section A is 0.8L, and the designed hydraulic retention time is 0.5h; the aeration tank in section B is designed according to the hydraulic retention time of 3.3h, and the corresponding effective volume is 7L ; Section A sedimentation tank and B section sedimentation tank have the same structure, both of which are vertical flow sedimentation tanks. The effective volume of the A section sedimentation tank is 3.5L and the residence time is 1.7h. The design hydraulic retention time of the sedimentation tank in sect...
Embodiment 2
[0043] Combine image 3 The present invention is further described with Example 2. The aeration tanks of section A and section B of the reaction device 1 are both loaded with activated sludge. Dissolved oxygen (DO) was monitored by a dissolved oxygen meter, and the DO value was maintained at 1.5~2.5g / L in the aeration tank of section A and 2.5~3.5g / L in the aeration tank of section B. The remaining operating conditions were the same as those in Example 1. The same. The A section and B section of the process are operated independently by adjusting the water pipe. The water volume of section A is 6.5L / d, the residence time is 3h, the water volume of section B is 50L / d, and the residence time is 3.3h. The reaction device 2 used the activated sludge in the reaction device 1 in Example 1. Both reactors 1 and 2 continuously process simulated domestic sewage with a COD / N of 6 until a stable removal rate of COD, ammonia nitrogen and total nitrogen is obtained. Then according to the...
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