Method and device for joint denitrifying by denitrification and anaerobic ammonia oxidation embedding particles
An anaerobic ammonium oxidation and denitrification technology, applied in chemical instruments and methods, anaerobic digestion treatment, biological treatment devices, etc., can solve problems such as low activity and incomplete denitrification, and achieve reduced inhibition, fast startup, The effect of high resistance to shock loads
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Embodiment 1
[0043] Example 1: A device for combined denitrification using denitrification and anammox embedding particles, such as figure 1 , the reaction device is cylindrical, divided into two independent areas inside and outside, the inner area is the reaction area, the outer area is the water bath area (5), the water bath area is the reaction area to maintain the temperature of the reaction area, and the outside of the water bath area is anaerobic ammonia The heat preservation and shading cover (6) of the oxidation reactor; the water inlet pipe (1) of the reaction zone is connected with the water inlet peristaltic pump, and the water inlet pipe of the reaction zone leads to the bottom of the reaction zone; the outlet of the reaction zone passes through the grid (8) and the reaction zone The area outlet pipe (2) is connected; the anaerobic ammonium oxidation embedding particles (10) in the reaction area are embedded in the Pall ring (9) or float in the reactor, and the denitrification e...
Embodiment 2
[0044] Example 2: Using WPU as a carrier to embed denitrifying bacteria and anammox bacteria respectively, and then place them together in the reaction device of Example 1 to realize the coupled denitrification of denitrification and anammox processes The operation method, the specific steps are as follows:
[0045] (1) Separation and selection of denitrifying bacteria
[0046] Take the backflow sludge from the secondary settling tank of the sewage treatment plant, pass through a 30-mesh nylon fine mesh, filter out the larger magazine particles, and then wash and centrifuge 2-3 times with 0.9% normal saline (each centrifuge at a speed of 4000r / min , 10 minutes each time), the enriched activated sludge was domesticated and cultivated with the prepared simulated nitrate nitrogen wastewater, and the simulated wastewater composition was: NaNO 3 :75mg / L, CH 3 COONa: 300mg / L, KH 2 PO 3 : 12.8mg / L, MgSO4: 10mg / L, ZnSO 4 ˙7H 2 O:3.5mg / L, CaCl 2 ˙2H 2 O:7.8mg / L, FeCl 2 ˙2H 2 ...
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