Rapid starting method of anaerobic ammonia oxidation reactor for enhancing sludge hydrolysis
An anammox, rapid start-up technology, which is applied in the field of rapid start-up of anammox reactors, can solve the problems of unfavorable growth and proliferation of anammox bacteria, slow start-up of anammox reactors, and obstacles to anammox Oxidative bacteria expansion and other issues, to shorten the start-up time, accelerate hydrolysis and autolysis, reduce the number and density of the effect
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Embodiment 1
[0034] 1L of anaerobic granular sludge was retrieved from the IC reactor of a wastewater treatment station in a paper mill. The measured particle size was 2.5±0.4mm, the density was 1.081±0.055g / mL, and the settling velocity was 36.7±3.8m / h. Wash the retrieved granular sludge three times with phosphate buffer (1mmol / L, pH 7), put it into a 2L container, add ammonia at a concentration of 120mg / L, and a nitrite concentration of 150mg / L (both in nitrogen Stir for 10 minutes, pass through argon gas for 30 minutes, seal it and let it stand in a dark place for 1 day. After it stinks and turns black, pour off the supernatant and continue to rinse with phosphate buffer for 3 times. The washed granular sludge is then repeated 2 times to complete the pretreatment. The pretreated sludge was inoculated into an anaerobic ammonium oxidation UASB reactor with a total volume of 2.5L and a reaction zone volume of 1.1L. The initial influent matrix ammonia and nitrite concentrations were set to ...
Embodiment 2
[0036]Anaerobic granular sludge was taken from a brewery wastewater treatment station. The average particle size was 1.7mm, the average density was 1.056g / mL, the sedimentation velocity was 26.4m / h, the concentration of ammonia added was 150mg / L, and the nitrite The concentration is 170mg / L; during the start-up process of the UASB reactor, the initial concentration of ammonia and nitrite in the influent substrate is set to be 180mg / L, both calculated as nitrogen, the initial hydraulic retention time is 5h, and the rising flow rate of the liquid surface in the reaction zone is 10.19 cm / h, during operation, slowly add 2.0g / L potassium bicarbonate solution from the bottom of the reactor through a peristaltic pump (the flow rate is 35mL / (L d)), slowly add 3.5mmol from the middle of the reactor / L dilute hydrochloric acid solution (flow velocity is 26mL / (L·d)).
[0037] All the other conditions are the same as in Example 1.
[0038] In the first 6 days of the reactor start-up proc...
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