Method for realizing nitrogen and phosphorus removal by quickly starting SBR (Sequencing Batch Reactor) system
A system implementation and quick start technology, applied in chemical instruments and methods, water treatment parameter control, water/sludge/sewage treatment, etc. Active, enhanced utilization effect
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Embodiment 1
[0031] The laboratory builds a set of SBR system, including 3 plexiglass reactors with an effective volume of 5L, the concentration of ammonia nitrogen is 200mg / L, the concentration of total nitrogen is 230mg / L, the concentration of COD is 500mg / L, and the concentration of total phosphorus is 15mg / L L of sewage.
[0032] First, inoculate the remaining activated sludge containing nitrifying bacteria and denitrifying phosphorus-accumulating bacteria in the secondary sedimentation tank of a certain sewage field according to the sludge concentration of 3000mg / L, and set an operating cycle of each reactor as 8h, in which the water is fed at the same time react. A single SBR reactor is carried out according to the first aeration reaction-the first stirring reaction-the second aeration reaction-sedimentation-drainage process. Each operation cycle is to add asparagine at 0.01mg / L in the initial stage of the first aeration reaction, and add rhamnose ester at 0.01mg / L in the first stir...
Embodiment 2
[0046] The reactor and start-up process and conditions are the same as in Example 1, except that in the stirring reaction stage, when the dissolved oxygen is reduced to less than 0.1 mg / L, betaine is added at a concentration of 0.1 mg / L to replace equal-quality phosphorylcholine alkali.
[0047] After the start-up of the SBR system is completed, the ratio of aeration time to stirring time in the last operating cycle is 3:1, when the removal rate of ammonia nitrogen in the influent reaches 94.4%, the removal rate of total nitrogen and total phosphorus reaches 85.1% and 86.2% respectively, start The period is 42 days.
Embodiment 3
[0049] The reactor, start-up process and conditions are the same as in Example 1, except that in the stirring reaction stage, trehalose ester is used to replace rhamnose ester of equal mass, and betaine is used to replace phosphorylcholine of equal mass.
[0050] After the start-up of the SBR system is completed, the ratio of the aeration time to the stirring time in the last operating cycle is 3:1, when the removal rate of ammonia nitrogen in the influent reaches 94.1%, the removal rate of total nitrogen and total phosphorus reaches 84.8% and 85.3% respectively, start The period is 43 days.
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