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 of AB process, can solve the problems of lack of efficient denitrification and failure to meet discharge requirements, achieve the goal of guaranteed denitrification, increase daily treatment capacity, sludge The effect of performance improvement
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Embodiment 1
[0031] In this embodiment, the method of the present invention and the common AB sewage treatment method are compared with each other. Reaction device 1 is an AB process reaction device that uses PCN series microorganism enhancement, and reaction device 2 is a reaction device of ordinary AB process.
[0032] All reactors of the AB process are made of plexiglass, see image 3 As shown, the design 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 ; The sedimentation tank of section A and the sedimentation tank of section B have the same structure, both are vertical flow sedimentation tanks, the effective volume of the sedimentation tank of section A is 3.5L, and the residence time is 1.7h. The design hydraulic retention time of the B section sed...
Embodiment 2
[0043] combine image 3 The present invention is further described with embodiment 2. The aeration tanks of section A and section B of the reaction device 1 are loaded with activated sludge. Dissolved oxygen (DO) is monitored by a dissolved oxygen measuring instrument, and the DO value maintained in the A section aeration tank is 1.5~2.5g / L, and the B section aeration tank is 2.5~3.5g / L, and all the other operating conditions are the same as in Example 1 in the same. The A section and B section of the process are operated independently by adjusting the water pipe. The water volume of the A section is 6.5L / d, and the residence time is 3h. The water volume of the B section is 50L / d, and the residence time is 3.3h. The reaction device 2 is equipped with activated sludge according to the reaction device 1 in the embodiment 1. Reactors 1 and 2 both continuously treat simulated domestic sewage with a COD / N ratio of 6 until a stable removal rate of COD, ammonia nitrogen and total ...
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