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

Inactive Publication Date: 2016-05-04
BEIJING UNIV OF CIVIL ENG & ARCHITECTURE
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0002] In the past 20 years, my country's domestic sewage treatment technology has made great progress. In municipal sewage treatment, nitrogen and phosphorus removal is generally taken as the main goal. In order to achieve the goal of simultaneous nitrogen and phosphorus removal, activated sludge method Based on the development of a large number of related processes including A 2 / O, SBR, CASS, etc. Although these methods can obtain good nitrogen and phosphorus removal effects, they all have the advantages of large area, high one-time investment, low resistance to low temperature, troubled by filamentous expansion, not only complicated management , will also produce a large amount of activated sludge. At the same time, some processes require external carbon source addition and chemical reagents to remove phosphorus, which greatly increases the cost of the process, which greatly limits the promotion and use of these processes in vast areas of our country.

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  • Sequencing batch adsorption aerating filter and slow rate soil infiltration tank coupling device and application thereof

Examples

Experimental program
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Effect test

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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Abstract

The invention discloses a sequencing batch adsorption aerating filter and slow rate soil infiltration tank coupling device and an application thereof to sewage treatment. The device comprises a concentration tank, a WAR (wet air regeneration) reactor, a heat exchanger, a PACT (powdered activated carbon treatment) tank, ammonia nitrogen aeration biosorption filters, a sewage return tank, a sewage denitrification tank, a deep phosphorus adsorption filter and a slow rate soil infiltration tank, wherein the concentration tank is connected with the WAR reactor; the WAR reactor is connected with the heat exchanger; the heat exchanger is connected with the PACT tank; the PACT tank is connected with the concentration tank and the ammonia nitrogen aeration biosorption filters; the ammonia nitrogen aeration biosorption filters are connected with the sewage return tank, the sewage denitrification tank and the deep phosphorus adsorption filter; the deep phosphorus adsorption filter is connected with the slow rate soil infiltration tank. The device can achieve the effects of removing pollutants in sewage, substantially reducing energy consumption and cost in the treatment process and better completing the resource regeneration process.

Description

technical field [0001] The invention relates to a coupling device of a sequence batch adsorption aeration filter tank and slow soil infiltration, in particular to a device for advanced treatment of sewage combining physical adsorption, biofilm method and slow soil infiltration. The present invention also relates to the application of the device in sewage treatment, that is, the method for treating sewage with the above-mentioned device. Background technique [0002] In the past 20 years, my country's domestic sewage treatment technology has made great progress. In municipal sewage treatment, nitrogen and phosphorus removal is generally taken as the main goal. In order to achieve the goal of simultaneous nitrogen and phosphorus removal, activated sludge method Based on the development of a large number of related processes including A 2 / O, SBR, CASS, etc. Although these methods can obtain good nitrogen and phosphorus removal effects, they all have the advantages of large are...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F3/06
CPCC02F1/28C02F3/06C02F3/10C02F3/28C02F3/327C02F3/34C02F9/00C02F2301/08Y02W10/10
Inventor 袁冬海何江伟刘钰钦郭旭晶严陈玲
Owner BEIJING UNIV OF CIVIL ENG & ARCHITECTURE
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