Improved treatment system of activated sludge of urban sewage and starting method
A technology for treating system and urban sewage, applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. The effect of low SVI value, improved precipitation performance, and cost savings
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Embodiment 1
[0029] An intermediate pilot plant of an urban sewage secondary treatment system adopts the anaerobic / anoxic / aerobic (A2 / O) biological treatment method to remove nitrogen and phosphorus. The COD concentration of urban sewage entering the secondary treatment system is 200-300mg / L. Total nitrogen 30-40mg / L, total phosphorus 2-4mg / L. If the traditional synchronous start-up process is adopted, the sludge concentration of the biological treatment system will only be 300-500 mg / L after 30 days of start-up, and the denitrification and phosphorus removal efficiency cannot meet the requirements. After adding 30mg / L flocculant (polyaluminum chloride), the sludge concentration increased slowly until the sludge concentration reached 1500mg / L after 2 months, but the sludge floc structure was loose and the activity was low.
[0030] Adopt the urban sewage denitrification and dephosphorization (A2 / O method) starting method with quick start function of the present invention, as figure 1 and ...
Embodiment 2
[0037] An intermediate pilot plant of an urban sewage secondary treatment system adopts the anaerobic / anoxic / aerobic (A2 / O) biological treatment method to remove nitrogen and phosphorus. The COD concentration of urban sewage entering the secondary treatment system is 200-300mg / L. Total nitrogen 30-40mg / L, total phosphorus 2-4mg / L. Processing methods such as image 3 shown. Its processing step 1, step 3 and step 4 are identical with embodiment 1. Step 2 is as follows:
[0038] Part of the sludge settled in the primary sedimentation tank is subjected to physical crushing pretreatment, and the size range of the crushed sludge is less than 1mm, and then used as the inoculation sludge of the secondary biological treatment system, and injected regularly and quantitatively through the primary sludge return system In the anaerobic tank of the secondary treatment system; the inoculation amount is intermittent, twice a day, each time the inoculation amount is 1 / 20 to 1 / 40 of the tota...
Embodiment 3
[0041] An intermediate pilot plant of an urban sewage secondary treatment system adopts anaerobic / aerobic (A / O) biological treatment method to carry out biological phosphorus removal of urban sewage. The concentration of COD entering the biological treatment system is 250-300 mg / L, and the concentration of total phosphorus 3 to 4 mg / L. Processing methods such as Figure 4 shown.
[0042] Concrete processing steps of the present invention are as follows:
[0043] (1) Urban sewage first passes through the grid and the primary settling tank for the first-level treatment system, and the sludge deposited in the primary settling tank is the primary sludge;
[0044] (2) Part of the sludge settled in the primary sedimentation tank is injected into the anaerobic tank of the biological treatment system in a regular and quantitative manner through the primary sludge return system, and inoculated. The primary sludge return system is composed of a sludge pump 1, a sludge pipeline 2 and ...
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