Serial composite fixed biofilm and activated sludge autotrophic denitrification apparatus and method on basis of continuous flow AAO phosphorus removal and partial denitrification
An activated sludge and autotrophic denitrification technology, applied in biological treatment devices, chemical instruments and methods, biological water/sewage treatment, etc., can solve the problems of nitrogen and phosphorus effluent being difficult to meet the standards at the same time, increasing operating costs, and consuming organic matter.
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specific Embodiment approach 1
[0030] Specific implementation mode one: combine figure 1 As shown, the present embodiment relates to a kind of compound fixed biofilm-activated sludge autotrophic denitrification device based on continuous flow A / A / O dephosphorization and partial denitrification series, which is characterized in that the main body of the process is composed of urban sewage raw water tank ( 1), a continuous flow A / A / O dephosphorization partial denitrification device (2), an intermediate water tank (3), and a composite fixed biofilm-activated sludge autotrophic denitrification device (4) consist of four parts; Water inlet pipe (1.1), overflow pipe (1.2) and vent pipe (1.3) are set on the urban sewage raw water tank (1); described continuous flow A / A / O dephosphorization and partial denitrification device (2) It is divided into four areas by the open-hole partition, which are anoxic area (2.1), anaerobic reaction area (2.2), two-stage aerobic reaction area (2.3) and precipitation area (3) in sequ...
specific Embodiment approach 2
[0031] Specific embodiment two: This embodiment relates to an application method based on continuous flow A / A / O dephosphorization and partial denitrification series compound fixed biofilm-activated sludge autotrophic denitrification device, which is carried out according to the following steps:
[0032] 1. Inoculation sludge stage
[0033] Inoculate the phosphorus removal sludge in the continuous flow A / A / O phosphorus removal and partial nitrogen removal reactor, control the sludge concentration MLSS to 2000-4000mg / L, take the actual urban domestic sewage as the treatment object, and the sludge reflux ratio is 100 %-150%, the DO concentration in the aerobic reaction zone is not less than 2mg / L. The design value of hydraulic retention time is 0.5-1.0h in the anoxic zone, 0.5-1.0h in the anaerobic zone, 1.5-2.5h in the aerobic zone, and the sludge age SRT is 3-5d. The shorter HRT and SRT ensure continuous The phosphorus-accumulating bacteria in the flow A / A / O phosphorus removal...
specific Embodiment approach 3
[0042] Specific embodiment 3: The difference between this embodiment and the specific embodiment is that the perforated partitions are connected to each compartment by staggering upper and lower flow holes according to the direction of water flow; the sedimentation tank adopts a vertical flow type The upper part of the sedimentation tank is cylindrical, and the sludge bucket is a truncated inverted cone with an inclination angle of 60°. It adopts the method of central water inlet and peripheral triangular weir outlet. Other steps and parameters are the same as those in Embodiment 1.
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