Sequencing batch adsorption aerating filter and slow rate soil infiltration tank coupling device and application thereof
A soil infiltration and aeration filter technology, which is applied in the fields of adsorption water/sewage treatment, multi-stage water treatment, water/sludge/sewage treatment, etc. and other problems, to achieve the effects of stable water quality, reduced energy consumption, and good application prospects
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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 slow soil infiltration, it comprises: concentration pond 1, WAR reactor 2, heat exchanger 10, PACT pond 3, ammonia nitrogen aeration biosorption Filter 4, sewage return pool 5, sewage denitrification pool 6, deep phosphorus adsorption filter 7 and slow 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, the ammonia nitrogen aeration The air 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 the slow soil infiltrati...
Embodiment 2
[0065] Please also refer to figure 1 As shown, the coupling device of the sequence batch adsorption aeration filter and slow soil infiltration in this embodiment includes: a concentration tank 1, a WAR reactor 2, a heat exchanger 10, a PACT tank 3, and ammonia nitrogen aerated organisms Adsorption filter 4, sewage reflux pool 5, sewage denitrification pool 6, deep phosphorus adsorption filter 7 and slow soil infiltration 8; wherein, the concentration pool 1 is connected to the WAR reactor 2, and the WAR reaction The device 2 is connected to the heat exchanger 10, and the heat exchanger 10 is connected to the PACT pool 3, and the PACT pool 3 is respectively connected to the concentration pool 1 and the ammonia nitrogen aerated biosorption filter 4, and the ammonia nitrogen The aerated biological adsorption filter 4 is respectively connected to the sewage return pool 5, the sewage denitrification tank 6 and the deep phosphorus adsorption filter 7, and the deep phosphorus adsorpt...
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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