Method for reducing excess sludge of aerobic unit of sewage treatment system by activated sludge process
A technology of sewage treatment system and activated sludge method, which is applied in water/sludge/sewage treatment, sludge treatment, biological sludge treatment, etc., can solve the problem of reduced sludge activity and achieve the effect of strong performance
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Embodiment 1~8、 comparative example 1~2
[0029] The treated sewage is oil refinery sewage, which is treated by oil separation and coagulation flotation. The quality of the influent water is:
[0030] COD575mg / l
[0031] pH 8.2
[0032] Sequenced batch activated sludge process (SBR process) is used for treatment, and the reactor volume is 8m3. The process includes: water inflow-aerobic reaction-sedimentation-decanting water-anaerobic (reciprocating), the operation of aerobic reaction process The process conditions are:
[0033] Sludge load 0.4~0.9kgBOD 5 / (kgMLVSS·d)
[0034] Reaction temperature 20~30℃
[0035] Dissolved oxygen 2~4mg / l
[0036] The amount of uncoupling agent added in sewage is shown in Table 2
[0037] (calculated in TCS)
[0038] The composition of the uncoupling agent that embodiment 1~8, comparative example 1~2 adopts comprises TCS, all the other components and proportioning ratio are listed in table 1, and the specific surface area of diatomite used is 30~60m 2 / g, the particle size of ...
Embodiment 9~16
[0040] The treated sewage is ethylene glycol production sewage, and the quality of the influent water is:
[0041]COD 2050mg / l
[0042] pH value 6~9
[0043] The AB activated sludge process is used for treatment, and the process includes in turn: water inflow-high-load aerobic treatment in section A-intermediate sedimentation tank-low-load aerobic treatment in section B-final sedimentation tank-drainage, intermediate sedimentation tank and final sedimentation tank Part of the sludge is returned to the respective aerobic tanks, and the remaining sludge is discharged. Embodiments 9 to 16 carry out sludge reduction treatment for the high-load aerobic unit of section A with high sludge yield (including high-load aerobic treatment and intermediate sedimentation tank of section A), and the operating process conditions are:
[0044] Sludge load 2~4kgBOD 5 / (kgMLVSS·d)
[0045] Reaction temperature 20~30℃
[0046] Dissolved oxygen 0.5~1mg / l
[0047] The amount of uncoupling agen...
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