CN2835234Y - Integrated denitrogenation and dephosphorization biofilter - Google Patents
Integrated denitrogenation and dephosphorization biofilter Download PDFInfo
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- CN2835234Y CN2835234Y CN 200520086738 CN200520086738U CN2835234Y CN 2835234 Y CN2835234 Y CN 2835234Y CN 200520086738 CN200520086738 CN 200520086738 CN 200520086738 U CN200520086738 U CN 200520086738U CN 2835234 Y CN2835234 Y CN 2835234Y
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Abstract
The utility model relates to an integrated denitrogenation and dephosphorization biological filter which belongs to the technical field of water treatment by taking the biological filter as a main body. A sewage treatment layer is composed of an anaerobic layer, a hypoxia layer and an aerobic layer, wherein the anaerobic layer is arranged on a supporting buffer layer; the hypoxia layer and the aerobic layer are orderly arranged on the anaerobic layer; baffles are arranged among the anaerobic layer, the hypoxia layer and the aerobic layer. A return pipe is arranged between the upper part of the aerobic layer and the lower part of the hypoxia layer; the lower part of the aerobic layer is provided with an aeration device which is connected with an aeration pump by an aeration pipe. The utility model changes the traditional structure provided with a single sewage treatment layer, combines the anaerobic layer, the hypoxia layer and the aerobic layer into the same reactor and integrates a nitration unit, a denitrification unit and a dephosphorization unit into the biological filter. The utility model has the advantages of high-efficiency denitrogenation and dephosphorization capability, shock and load resistance, stable running, few occupied land, low capital construction and running cost, simple and convenient management and operation, etc.
Description
(1) technical field
The utility model relates to a kind of integration denitrification and dephosphorization biological filter, belongs to the water treatment field technology based on the biological filter.
(2) background technology
Along with development of industry and agriculture, the dead front type waters eutrophication phenomenon that a large amount of high nitrogen and phosphorus content sewage emissions cause is on the rise.As traditional biological denitrification method, denitrification reaction generally need be through two bioprocesses: nitration reaction and denitrification process, the nitrification and denitrification reaction must independently be finished in the operating unit respectively.This technology relates to three lock out operation unit, two return-flow systems; For small scall scale city and industrial sewage, then too huge, complicated, floor space is big.At present some novel denitrification dephosphorization techniques are as appearance such as synchronous nitration and denitrifications, and these technology can be saved organic carbon source in a large number, save energy consumption, but that is that all right is ripe for these technology, applies also having difficulties.
The biological filter is a kind of traditional water treatment device, it is simple to have technology, floor space is little, the characteristics that capital construction and working cost are low, it is single anaerobic layer or single layer of oxygen deficient or single aerobic layer that but its sewage disposal layer is generally form, can not realize denitrogenation effectively, filling adsorption poor performance commonly used can't realize effective dephosphorization.
(3) summary of the invention
The integration denitrification and dephosphorization biological filter of advantages such as at the defective of prior art, the utility model provides a kind of high-efficient denitrification and dephosphorization ability that has, and anti-shock loading is stable, takes up an area of to lack, and capital construction and working cost are low, and bookkeeping is simple and convenient.
A kind of integration denitrification and dephosphorization biological filter, comprise water inlet pipe, rising pipe, support buffer layer and sewage disposal layer, the sewage disposal layer is made up of anaerobic layer, layer of oxygen deficient and aerobic layer, anaerobic layer is arranged on the support buffer layer, be layer of oxygen deficient and aerobic layer successively above the anaerobic layer, be respectively equipped with dividing plate between anaerobic layer, layer of oxygen deficient and the aerobic layer.
Aerobic layer top and and the layer of oxygen deficient bottom between be provided with return line.
The aerobic layer bottom is provided with an aerating apparatus, and this aerating apparatus is under the dividing plate between layer of oxygen deficient and the aerobic layer; This aerating apparatus is connected with aeration pump by aeration tube.
The utility model has changed traditional structure that single sewage disposal layer is set, melt anaerobic layer, layer of oxygen deficient and aerobic layer in same reactor, with nitrated unit, denitrification unit and dephosphorization unit are incorporated in the biological filter, the top of biological filter is aerobic layer, the middle part is a layer of oxygen deficient, and the bottom is an anaerobic layer.The filler of reactor is that shell or oyster shells etc. contain the cheap material that enriches calcium salt.Sewage is flowed into by the bottom, forms one section anaerobic layer; Water outlet is flowed out by top, is partly refluxed to the middle part, forms one section layer of oxygen deficient; The aerobic layer bottom is provided with aerating apparatus, the sewage anaerobic layer of flowing through successively, and layer of oxygen deficient and aerobic layer, filler and microorganism carry out double purified to sewage, finish to organism the removal of nitrogen and phosphorus.
The utlity model has the high-efficient denitrification and dephosphorization ability, anti-shock loading, stable, take up an area of few, advantage such as capital construction and working cost are low, and bookkeeping is simple and convenient.
(4) description of drawings
Fig. 1 is a structural representation of the present utility model.
Wherein, 1, water inlet pipe, 2, the support buffer layer, 3, anaerobic layer, 4, layer of oxygen deficient, 5, dividing plate, 6, aerobic layer, 7, aeration pump, 8, aeration tube, 9, rising pipe, 10, aerating apparatus, 11, return line.
(5) embodiment
Embodiment: structure of the present utility model as shown in Figure 1, comprise water inlet pipe 1, rising pipe 11, support buffer layer 2 and sewage disposal layer, the sewage disposal layer is made up of anaerobic layer 3, layer of oxygen deficient 4 and aerobic layer 6, anaerobic layer 3 is arranged on the support buffer layer 2, be layer of oxygen deficient 4 and aerobic layer 6 successively above the anaerobic layer 3, be respectively equipped with dividing plate 5 between anaerobic layer 3, layer of oxygen deficient 4 and the aerobic layer 6.Aerobic layer 6 tops and and layer of oxygen deficient 4 bottoms between be provided with return line 11.Aerobic layer 6 bottoms are provided with an aerating apparatus 10, the dividing plate of this aerating apparatus 10 between layer of oxygen deficient 4 and aerobic layer 65 times; This aerating apparatus 10 is connected with aeration pump 7 by aeration tube 8.
Claims (3)
1, a kind of integration denitrification and dephosphorization biological filter, comprise water inlet pipe, rising pipe, support buffer layer and sewage disposal layer, it is characterized in that, the sewage disposal layer is made up of anaerobic layer, layer of oxygen deficient and aerobic layer, anaerobic layer is arranged on the support buffer layer, be layer of oxygen deficient and aerobic layer successively above the anaerobic layer, be respectively equipped with dividing plate between anaerobic layer, layer of oxygen deficient and the aerobic layer.
2, integration denitrification and dephosphorization as claimed in claim 1 biological filter is characterized in that, is provided with return line between described aerobic layer top and the layer of oxygen deficient bottom.
3, integration denitrification and dephosphorization as claimed in claim 1 biological filter is characterized in that described aerobic layer bottom is provided with an aerating apparatus, and this aerating apparatus is under the dividing plate between layer of oxygen deficient and the aerobic layer; This aerating apparatus is connected with aeration pump by aeration tube.
Priority Applications (1)
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CN 200520086738 CN2835234Y (en) | 2005-09-09 | 2005-09-09 | Integrated denitrogenation and dephosphorization biofilter |
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CN 200520086738 CN2835234Y (en) | 2005-09-09 | 2005-09-09 | Integrated denitrogenation and dephosphorization biofilter |
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CN2835234Y true CN2835234Y (en) | 2006-11-08 |
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CN 200520086738 Expired - Fee Related CN2835234Y (en) | 2005-09-09 | 2005-09-09 | Integrated denitrogenation and dephosphorization biofilter |
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100410189C (en) * | 2006-12-07 | 2008-08-13 | 同济大学 | Nitration denitrification integral type sewage denitrification biomembrane reactor |
CN101844858A (en) * | 2010-06-17 | 2010-09-29 | 北京交通大学 | Aerobic-anoxic-anaerobic integrated module type sewage fast denitrogenation reactor and treatment method thereof |
CN102001802A (en) * | 2010-12-31 | 2011-04-06 | 上海交通大学 | Nitrification and denitrification combined integral biological filter |
CN102145960A (en) * | 2011-02-24 | 2011-08-10 | 江苏省环境科学研究院 | Device and method for denitrifying and dephosphorizing ecological protection multi-level filtration wall in water source area on rural land surface |
CN102874924A (en) * | 2012-08-31 | 2013-01-16 | 惠州市新明水务工程有限公司 | Novel ammonia nitrogen biotreatment device |
CN103496786A (en) * | 2013-10-22 | 2014-01-08 | 南京大学 | Low-energy-consumption denitrification biological filter and treatment method thereof |
CN103708617A (en) * | 2014-01-17 | 2014-04-09 | 安徽锋亚环境技术有限公司 | Assembled stereoscopic A2/O reaction tank for rural dispersible sewage treatment |
CN104529091A (en) * | 2015-01-08 | 2015-04-22 | 北京中瑞佳亿环境科技有限公司 | Sewage treatment device and method for micro-power multi-medium fixed biological filter |
CN105417691A (en) * | 2014-09-18 | 2016-03-23 | 重庆大学 | Construction method for denitrifyjng simultaneous phosphorus and nitrogen removal advanced treatment system of anoxic biological filter |
CN110330171A (en) * | 2019-06-19 | 2019-10-15 | 苏州市清泽环境技术有限公司 | A kind of efficient denitrification reactor |
CN112875979A (en) * | 2020-12-31 | 2021-06-01 | 南京化工园博瑞德水务有限公司 | Biodegradation device for wastewater containing hydroxyethyl cellulose and addition product thereof |
CN114349267A (en) * | 2021-12-17 | 2022-04-15 | 江西零真生态环境集团有限公司 | AO coupling biological filter domestic sewage treatment system and process |
-
2005
- 2005-09-09 CN CN 200520086738 patent/CN2835234Y/en not_active Expired - Fee Related
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100410189C (en) * | 2006-12-07 | 2008-08-13 | 同济大学 | Nitration denitrification integral type sewage denitrification biomembrane reactor |
CN101844858A (en) * | 2010-06-17 | 2010-09-29 | 北京交通大学 | Aerobic-anoxic-anaerobic integrated module type sewage fast denitrogenation reactor and treatment method thereof |
CN101844858B (en) * | 2010-06-17 | 2011-11-09 | 北京交通大学 | Aerobic-anoxic-anaerobic integrated module type sewage fast denitrogenation reactor and treatment method thereof |
CN102001802A (en) * | 2010-12-31 | 2011-04-06 | 上海交通大学 | Nitrification and denitrification combined integral biological filter |
CN102145960A (en) * | 2011-02-24 | 2011-08-10 | 江苏省环境科学研究院 | Device and method for denitrifying and dephosphorizing ecological protection multi-level filtration wall in water source area on rural land surface |
CN102145960B (en) * | 2011-02-24 | 2012-11-14 | 江苏省环境科学研究院 | Device and method for denitrifying and dephosphorizing ecological protection multi-level filtration wall in water source area on rural land surface |
CN102874924A (en) * | 2012-08-31 | 2013-01-16 | 惠州市新明水务工程有限公司 | Novel ammonia nitrogen biotreatment device |
CN103496786B (en) * | 2013-10-22 | 2015-06-17 | 南京大学 | Low-energy-consumption denitrification biological filter and treatment method thereof |
CN103496786A (en) * | 2013-10-22 | 2014-01-08 | 南京大学 | Low-energy-consumption denitrification biological filter and treatment method thereof |
CN103708617A (en) * | 2014-01-17 | 2014-04-09 | 安徽锋亚环境技术有限公司 | Assembled stereoscopic A2/O reaction tank for rural dispersible sewage treatment |
CN105417691A (en) * | 2014-09-18 | 2016-03-23 | 重庆大学 | Construction method for denitrifyjng simultaneous phosphorus and nitrogen removal advanced treatment system of anoxic biological filter |
CN104529091A (en) * | 2015-01-08 | 2015-04-22 | 北京中瑞佳亿环境科技有限公司 | Sewage treatment device and method for micro-power multi-medium fixed biological filter |
CN110330171A (en) * | 2019-06-19 | 2019-10-15 | 苏州市清泽环境技术有限公司 | A kind of efficient denitrification reactor |
CN112875979A (en) * | 2020-12-31 | 2021-06-01 | 南京化工园博瑞德水务有限公司 | Biodegradation device for wastewater containing hydroxyethyl cellulose and addition product thereof |
CN114349267A (en) * | 2021-12-17 | 2022-04-15 | 江西零真生态环境集团有限公司 | AO coupling biological filter domestic sewage treatment system and process |
CN114349267B (en) * | 2021-12-17 | 2022-10-28 | 江西零真生态环境集团有限公司 | AO coupling biological filter domestic sewage treatment system and process |
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20061108 |