System and method for accumulating nitrite nitrogen in partial nitrification process
A short-range nitrification and nitrous nitrogen technology, applied in the field of ammonia nitrogen-containing sewage treatment, can solve the problems of poor operation stability and inconvenient system operation, and achieve the effects of small footprint, short process flow and high efficiency
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Embodiment 1
[0036] like figure 1As shown, the system structure of the present invention includes a stirred upflow reaction 1, a vertical flow sedimentation tank 2, a water quality monitoring device, an aeration device and an acid-base adjustment device. Stirred upflow reactor 1 is a cylindrical reactor with an aspect ratio of 10-15, and a stirring device 3 is provided in the cylindrical reactor, and the stirring device 3 includes a stirring rod arranged along the axis of the stirred upflow reactor 1. Stirring blades distributed on the stirring rod and a speed controller connected with the stirring rod. During operation, the stirring device can be controlled at an appropriate stirring speed by the speed controller as required.
[0037] The bottom of the stirred upflow reactor 1 is connected to the water inlet tank 5 through the water inlet pipe 4, and the top of the stirred upflow reactor 1 is connected to the vertical flow sedimentation tank 2 through the reactor outlet pipe 6, and the ve...
Embodiment 2
[0042] The method for accumulating nitrous nitrogen in the short-range nitrification process of the present invention comprises the following steps:
[0043] a. Set up the above-mentioned system for accumulating nitrous nitrogen, wherein the height of the stirred upflow reactor is 115 cm, and the inner diameter is 9.5 cm.
[0044] b. Add digested sludge from the aeration tank of Baoding Sewage Treatment Plant to the stirred upflow reactor. After adding, the MLSS is 4189 mg / L, and the surface aeration head, pH probe, dissolved oxygen probe and oxidation The reduction potential probe is submerged 17cm below the liquid surface.
[0045] c. Acclimatization stage: the DO at the dissolved oxygen probe is controlled to be 0.6~0.7mg / L, the pH is 7.5~8.5, the ORP is 10~200mV, the temperature is 25~35°C, and the concentration of ammonia nitrogen is set to 150mg / L and ammonia nitrogen concentration of 50mg / L wastewater are alternately fed into the water for domestication until the ammon...
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