Coupling device of sequencing-batch adsorption aerating filter and underground soil infiltration device and application of coupling device
A soil infiltration and aeration filter technology, applied in multi-stage water treatment, water/sludge/sewage treatment, biological water/sewage treatment, etc., can solve high energy consumption, complex operation and management, and single treatment process and other issues, to achieve the effect of reducing energy consumption, good application prospects, and stable water quality
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Embodiment 1
[0045] Such as figure 1 As shown, the coupling device of the sequence batch type adsorption aeration filter of the present invention and underground soil infiltration includes: a concentration pool 1, a WAR reactor 2, a heat exchanger 10, a PACT pool 3, an ammonia nitrogen aeration biosorption filter pool 4, sewage reflux pool 5, sewage denitrification pool 6, deep phosphorus adsorption filter 7 and underground soil infiltration 8; wherein, the concentration pool 1 is connected to the WAR reactor 2, and the WAR reactor 2 is connected to The heat exchanger 10, the heat exchanger 10 is connected to the PACT pool 3, the PACT pool 3 is respectively connected to the concentration pool 1 and the ammonia nitrogen aerated biological adsorption filter 4, and the ammonia nitrogen aerated biological The adsorption filter 4 is respectively connected to the sewage reflux pool 5, the sewage denitrification tank 6 and the deep phosphorus adsorption filter 7, and the deep phosphorus adsorptio...
Embodiment 2
[0065] Please also refer to figure 1 As shown, the coupling device of the sequence batch adsorption aeration filter and underground soil infiltration in this embodiment includes: a concentration pool 1, a WAR reactor 2, a heat exchanger 10, a PACT pool 3, and ammonia nitrogen aeration biosorption Filter 4, sewage reflux pool 5, sewage denitrification pool 6, deep phosphorus adsorption filter 7 and underground soil infiltration 8; wherein, the concentration pool 1 is connected to the WAR reactor 2, and the WAR reactor 2 Connect the heat exchanger 10, the heat exchanger 10 is connected to the PACT pool 3, the PACT pool 3 is respectively connected to the concentration pool 1 and the ammonia nitrogen aerated biosorption filter 4, and the ammonia nitrogen aeration The biosorption filter 4 is respectively connected to the sewage reflux pool 5, the sewage denitrification pool 6 and the deep phosphorus adsorption filter 7, and the deep phosphorus adsorption filter 7 is connected to th...
Embodiment 3
[0085] Adopt the device described in embodiment 1 to carry out sewage treatment.
[0086] Sewage adopts the method of sequential batch water intake, and the time interval of water intake is 12 hours. The sewage enters the PACT pool 3, and the organic pollutants in the sewage are removed by the adsorption of powdered activated carbon in the PACT pool 3 and the biodegradation of biochemical sludge. into CO 2 and H 2 O, ammonia nitrogen is converted into nitrate nitrogen, and heavy metal ions are solidified and precipitated under the action of red mud molecular sieves to purify sewage; the supernatant of PACT pool 3 is introduced into ammonia nitrogen aerated biosorption filter 4, and ammonia nitrogen is absorbed by the natural After adsorption by zeolite or artificial zeolite (NH 3 -N removal rate can reach 99%), valve A is closed, valve B is opened, and the sewage flows into the sewage return pool 5 for storage. At the same time, add nitrifying bacteria to the ammonia nitrog...
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