Method of all self-oxygen ammonia nitrogen removal by particle sludge
A granular sludge and anaerobic granular sludge technology, applied in the field of ammonia nitrogen removal, can solve the problems of low sludge concentration and high investment and operation costs, achieve high microbial biomass, reduce operational difficulty and operating costs, and improve removal efficiency
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Embodiment 1
[0016] The aerobic sludge from the aeration tank of the urban sewage treatment plant and the anaerobic sludge from the concentration tank are mixed according to the mass ratio of 5:1, and then the mixed sludge is inoculated into the upflow aerobic sludge bed reactor; Configure the ammonia nitrogen concentration of simulated wastewater to be 500mg / L, add MgCl 2 The concentration is 20mg / L, the operating conditions of the reactor are: temperature 25-35°C, pH value 6.2-7.8, dissolved oxygen 2.5-5.3mg / L, hydraulic retention time 6-10 hours, air aeration , the air rate is 20-30L / h, and after 75 days of stable operation, brown aerobic denitrification granular sludge was observed in the reactor, with a particle size of 0.7-1.1mm and a density of 1.01-1.28g / cm 3 . At the same time, the removal rate of total nitrogen in wastewater reaches 82%.
Embodiment 2
[0018] Using the same inoculated sludge as in Example 1, the ammonia nitrogen concentration of artificially configured simulated wastewater is 500 mg / L, and MgCl is added 2 The concentration is 15mg / L, CaCl 2 The concentration is 5mg / L, and the brown aerobic denitrification granular sludge was observed in the reactor after 83 days of stable operation, with a particle size of 0.8-1.2mm and a density of 1.03-1.19g / cm 3 , At the same time, the removal rate of total nitrogen in wastewater reaches 85%.
Embodiment 3
[0020] The activated sludge from the sewage treatment system of a chemical fertilizer plant was used to inoculate into the upflow aerobic reactor, the total nitrate concentration of simulated wastewater was artificially configured to be 800mg / L, and the air velocity of the reactor was 30-45L / h. Other conditions and implementation The same as Example 1, after 89 days of continuous operation, brown aerobic denitrification granular sludge was observed in the reactor, with a particle size of 2.2-3.2mm and a density of 1.18-1.40g / cm 3 , The total nitrogen removal rate reached 89.5%.
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