Anaerobic ammonia oxidation and aerobic oxygen limited starting method based on MBBR (Moving Bed Biofilm Reactor)
An anammox and ammonia nitrogen technology, which is applied in the field of anaerobic ammonium oxidation and aerobic limited start-up based on MBBR, can solve the problems of high processing load, long start-up period, short start-up period, etc., and achieves high processing load and start-up speed. Fast, reliable results
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Embodiment 1
[0030] Step 1: The specific surface area of the suspended filler used in the MBBR process is ≥500m 2 / m 3 , the specific gravity is 0.95, the diameter is 25cm, the thickness is 10cm, and the reactor volume is 5m 3 , add suspended filler 2.50m 3 , filling rate is 50%;
[0031]Step 2: Anammox bacteria are not easy to form film on the filler, but nitrifying bacteria are easy to form film, and nitrifying bacteria are one of the sources of anammox bacteria, so start nitrification first. Nitrification start, the nitrification start is carried out when the water temperature is 20.1-20.4°C, the activated sludge in the aeration tank of the sewage treatment plant is inoculated, the sludge concentration in the reactor after inoculation is 3.88g / L, and the ammonia nitrogen removal load of the reactor is 0.056kgN / kgMLSS / d; put the inoculated sludge into the reactor and fully mix it with the biological filler, and run it intermittently. The concentration of ammonia nitrogen in the inf...
Embodiment 2
[0036] In order to verify the operation of MBBR-ANAMMOX under high ammonia nitrogen conditions, the total nitrogen membrane surface load reached 7.98gN / m in Example 1 until 214 days 2 / d, at this time the volume load is 1.99kgN / m 3 / d, after the system has matured and stabilized, continue the anaerobic operation, the anaerobic stirring power is 13W / m 3 , control influent ammonia nitrogen 270-275mg / L, influent nitrite nitrogen 315-330mg / L, influent pH 7.3-7.9, after 90 days the working condition of the reactor tends to be stable, and the total nitrogen membrane surface load reaches 20.83gN / m 2 / d, at this time the volumetric load is 5.21kgN / m 3 / d, the increase in load is more conducive to anammox due to high ammonia nitrogen.
[0037] From figure 1 , figure 2 , image 3 It can be seen that: the change of nitrogen during the whole anammox start-up process;
[0038] Figure 4 : The characteristic stoichiometric coefficient of the anammox reaction refers to the ratio of...
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