Startup and control method for multistage partial nitrification
A control method and nitrosation technology, applied in chemical instruments and methods, water treatment parameter control, water pollutants, etc., can solve problems such as difficulty in maintaining sludge concentration, unstable effluent nitrogen ratio, and difficulty in continuous flow operation. Achieve long-term stable operation, low energy consumption for aeration and fluidization, and high oxygen utilization rate
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[0061] The reactor pool capacity is 10m 3 , using a specific surface area of 700m 2 / m 3 Suspended carrier, the specific gravity of the suspended carrier before film formation is 0.965, and the porosity is >95%; the reactor is divided into 8 stages, and the reactors at each stage have the same tank capacity and the same filling rate, and no sludge reflux is set. The concentration of suspended sludge is always <0.5g / L; the influent is decarbonized domestic sewage, the influent BOD is 10±3mg / L, TN is 55±6mg / L, ammonia nitrogen is 50±5mg / L, BOD : TN<0.2, influent SS<20mg / L, water temperature is 14±2℃;
[0062] 1) Start nitrification, fill suspension carrier 4m 3 , the filling rate is 40%, the DO is controlled at 4-5mg / L, and the activated sludge of the sewage plant is inoculated with 4g / L. Sludge, start continuous water inflow and aeration, initial HRT=10h, DO control at 4-5mg / L, by 15d, ammonia oxidation rate is 72%, ammonia nitrogen removal surface load is 0.306gN / (m 2 ·...
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