Method based on MBBR for removing ammonia nitrogen from high hardness wastewater
A high-hardness, ammonia-nitrogen technology, applied in chemical instruments and methods, biological water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problems of unstable treatment effect, poor resistance to high salt, and difficulty in scaling , to achieve the effect of low energy consumption, fast start-up speed and reliable operation of aeration and fluidization
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Embodiment 1
[0024] 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 suspension filler 2.00m 3 , filling rate is 40%;
[0025] Start the inoculation, inoculate the activated sludge in the aeration tank of a sewage treatment plant, the sludge concentration after inoculation is 2.5g / L, and the ammonia nitrogen removal load of the reactor is 0.050kgN / kgMLSS / d; after inoculation, it operates in intermittent mode, and the water temperature is 15.7 ℃, by adding ammonium sulfate and sodium bicarbonate to the raw water, the concentration of ammonia nitrogen in the influent water is 109.33mg / L, the total alkalinity is 634.1mg / L (calculated as calcium carbonate), and the ratio of aeration air to water is 8.8. When the ammonia nitrogen consumption exceeds Stop the reaction at 90%, discharge all the water and sludge; add ammonium sulfate and s...
Embodiment 2
[0029] The specific surface area of the suspended filler used in the MBBR process is ≥620m 2 / m 3 , with a specific gravity of 0.95, a diameter of 25cm, a thickness of 10cm, and a reactor volume of 15m 3 , add suspended filler 4.80m 3 , filling rate is 32%;
[0030] Start the inoculation, inoculate the activated sludge in the aeration tank of a sewage treatment plant, the sludge concentration after inoculation is 2.5g / L, and the ammonia nitrogen removal load of the reactor is 0.052kgN / kgMLSS / d; after inoculation, it operates in intermittent mode, and the water temperature is 20.1 ℃, by adding ammonium sulfate and sodium bicarbonate to the raw water, the concentration of ammonia nitrogen in the influent water is 152.8mg / L, the total alkalinity is 1000.2mg / L, the ratio of aeration gas to water is 11.8, and the reaction is stopped when the consumption of ammonia nitrogen exceeds 90%. Drain all the water and sludge; re-intake water and add ammonium sulfate and sodium bicarbon...
Embodiment 3
[0034] The specific surface area of the suspended filler used in the MBBR process is ≥620m 2 / m 3 , with a specific gravity of 0.95, a diameter of 25cm, a thickness of 10cm, and a reactor volume of 15m 3 , add suspended filler 6.00m 3 , filling rate is 40%;
[0035] Start the inoculation, inoculate the activated sludge in the aeration tank of a sewage treatment plant, the sludge concentration after inoculation is 2.9g / L, and the ammonia nitrogen removal load of the reactor is 0.060kgN / kgMLSS / d; after inoculation, it operates in intermittent mode, and the water temperature is 23.7 ℃, by adding ammonium sulfate and sodium bicarbonate to the raw water, the concentration of ammonia nitrogen in the influent water is 161.3mg / L, the total alkalinity is 1212mg / L (calculated as calcium carbonate), and the ratio of aeration air to water is 14.1. When the ammonia nitrogen consumption exceeds 90 %, stop the reaction, discharge all the water and sludge; re-inflow and add ammonium sulf...
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