Double-membrane three-phase internal-circulation aeration biological fluidized bed and method for treating wastewater
A technology of three-phase internal circulation and biological aeration, applied in chemical instruments and methods, water aeration, sedimentation treatment, etc., can solve the problems of low removal rate of specific nutrients, easy shedding of biofilm, unscientific configuration, etc. , to achieve the effect of improving COD and total nitrogen removal efficiency, improving mass transfer effect, and strengthening denitrification effect
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Embodiment 1
[0051] Such as figure 1 As shown, a double-membrane three-phase internal circulation aerated biological fluidized bed has an internal and external double cylinder structure, including an aeration system 100, an internal circulation system 200, a fixed film reaction zone 300, and a sedimentation zone 510. The internal circulation system 200 includes a fluidized film reaction zone 230 formed by an outer cylinder 210 and an inner cylinder 220. There is a suspended spherical filler 240 in the fluidized membrane reaction zone 230. The suspended spherical filler 240 is composed of a double-layer structure of an outer shell and an inner core. The outer shell is made of polypropylene Hollow fish mesh spherical shell made of material injection molding, the inner core is a sponge-like porous polymer (see figure 2 ), such as commercially available suspended spherical fillers, which have the characteristics of strong bioadhesion, large specific surface area, high porosity, good chemical ...
Embodiment 2
[0066] The wastewater quality and operating conditions are the same as in Example 1. The difference is: in the internal circulation system 200, when the height-to-diameter ratio of the outer cylinder 210 is 4:1, the COD removal rate is 94%, and the ammonia nitrogen removal rate is 74% ( Figure 4 ).
Embodiment 3
[0068] The wastewater quality and operating conditions are the same as in Example 1. The difference is: in the internal circulation system 200, when the height-to-diameter ratio of the outer cylinder 210 is 6:1, the COD removal rate is 98%, and the ammonia nitrogen removal rate is 85% ( Figure 4 ).
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