CN203613023U - Alternating aeration filter bioreactor - Google Patents

Alternating aeration filter bioreactor Download PDF

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Publication number
CN203613023U
CN203613023U CN201320515918.0U CN201320515918U CN203613023U CN 203613023 U CN203613023 U CN 203613023U CN 201320515918 U CN201320515918 U CN 201320515918U CN 203613023 U CN203613023 U CN 203613023U
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CN
China
Prior art keywords
aeration
water
reaction chambers
serving
reaction
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201320515918.0U
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Chinese (zh)
Inventor
李秀东
邓念雄
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
HUBEI PANGU ENVIRONMENTAL PROTECTION ENG&TECH Co Ltd
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HUBEI PANGU ENVIRONMENTAL PROTECTION ENG&TECH Co Ltd
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Priority to CN201320515918.0U priority Critical patent/CN203613023U/en
Application granted granted Critical
Publication of CN203613023U publication Critical patent/CN203613023U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

The utility model discloses an alternating aeration filter bioreactor comprising a shell, wherein the shell comprises two reaction chambers, a water inlet (also serving as a water outlet) is formed in the bottom of each of the two reaction chambers, a mud discharging port is formed in the top of each reaction tank, and a water passing hole with a metal mesh is formed in the upper part of each of the two reaction tanks. A water distribution system (also serving as a water collecting system) is arranged at the inner bottom of each of the two reaction chambers, and an aeration system, a suspended packing area (also serving as a filtering area) and a residual sludge area are arranged upwards in sequence in the two reaction chambers. The suspended packing area (also serving as the filtering area) is filled with novel suspended fiber polyhedral balls, the diameter of each of the polyhedral balls is about 2.5cm, and the proportion of the balls is about 1.007; during aeration, all the polyhedral balls are suspended in water, and when aeration is stopped, the polyhedral balls are quickly settled and accumulated. The alternating aeration filter bioreactor disclosed by the utility model has a compact structure, occupies less space, can be used for performing biological treatment on urban domestic wastewater by using only one set of equipment, and is good in effluent quality, low in investment cost, high in degree of automation and very convenient in operation and maintenance. Moreover, the alternating aeration filter bioreactor integrates multiple techniques such as biochemical treatment and filtering, is strong in decontamination capability, high in reliability and safe and stable in effluent quality, and can completely reach the first-level standard A of urban sewage quality discharge.

Description

A kind of alternative aeration filtering biological reactor
Technical field
The utility model relates to municipal sanitary sewage disposal technical field, relates in particular to aeration filtration bio-reactor wherein.
background technology
City domestic sewage is the product in urban development, is accompanied by urbanization and industrialized high speed progress, and the generation of sanitary sewage is increasing, and environmental pollution seriously aggravates, and becomes a large important factor of restriction social economy sustainable development.What at present domestic and international sewage disposal technology, employing was the most general is exactly physico-chemical processes and biologic treating technique, and biologic treating technique is more extensive.At present, in sanitary sewage, the increase of pollutant kind and quantity and country cause most traditional technology cannot reach the index of defined for the raising of Pollution abatement index, face the difficult situation of being badly in need of transformation.So need to deepen traditional technology, optimisation technique parameter, improves effluent quality, cuts operating costs, and therefore sewage disposal technology need to be innovated raising in a hurry on conventional art, to tackle the demand of new markets.
Traditional BAF treatment technology, by certain technique means, allows fixing microorganic adhesion on carrier, makes microorganism set growth, larger surface-area is conducive to increase the quantity of microorganism, improve system processing power and adaptability, shorten the treatment time, reduce processing cost.But still there is a series of problem in BAF: during as aeration, filler and biomembranous filtering function can not be brought into play its effect completely, and not process the appropriate suspended substance that causes higher for the mutual relationship between bio-oxidation function and filtering function; In traditional backwash process, cause biomembranous big area to come off and the waste of backwash water etc.
summary of the invention
For the deficiency of traditional existing treatment technology of BAF, the utility model provides a kind of alternative aeration filtering biological reactor, to reach, effluent quality is good, investment operation cost is low, without back flushing, can realize the object of high-efficient denitrification and dephosphorization and the suspended substance removal of city domestic sewage.
For achieving the above object, the utility model provides a kind of alternative aeration filtering biological reactor, comprises housing, and described housing comprises two reaction chambers, and " aeration-filtration " according to the certain hour cycle, hockets.Two reaction chamber bottoms are equipped with cloth water gathering system, are upwards aerating system, floating stuffing district and excess sludge district successively.On this new suspended packing, a large amount of micropopulations in load, can carry out the organism in absorption degradation water.In the time of aeration, floating stuffing evenly suspends in water, and relies on microbial film degraded water pollutant; In the time stopping aeration, the rapid deposition of filler (filler proportion is greater than sewage proportion), forms good filtering layer.
The beneficial effects of the utility model are: biological reaction tank and filtration are organically combined in to one, compact construction, floor space is little, only needs a set of equipment city domestic sewage to be carried out a biological disposal upon, and effluent quality is good, cost of investment is low, level of automation is high, operation and maintenance is all very convenient.And device integrates biochemical treatment, filters, soil removability is strong, reliability is high, and effluent quality safety and stability, for BAF provides new technical scheme.Can be widely used in municipal sanitary sewage disposal field.
accompanying drawing explanation;
Fig. 1 is structural representation of the present utility model.
In figure: 1. housing; 2. water inlet pipe (the double rising pipe that does); 3. water distribution system (the double water gathering system of doing); 4. aeration tube; 5. bed course; 6. floating stuffing district (the double filtrating area of doing); 7. excess sludge district; 8. water hole; 9. shore pipe; 10. filtrating area (Jian Zuo floating stuffing district); 11. rising pipes (the double water inlet pipe that does); 12. dividing plates.
embodiment
Below in conjunction with drawings and Examples, the utility model is described in further detail.
Illustrated a kind of alternative aeration filtering biological reactor, housing 1 is divided into two reaction chambers by dividing plate 12, the bottom of described housing 1 is equipped with respectively water inlet pipe (the double rising pipe that does) 2, housing 1 inside is provided with water distribution system (the double water gathering system of doing) 3, aeration tube 4, bed course 5, floating stuffing district (the double filtrating area of doing) 6, excess sludge district 7, water hole 8, shore pipe 9, filtrating area (Jian Zuo floating stuffing district) 10, rising pipe (the double water inlet pipe that does) 11 successively along water (flow) direction (within a reaction time, in the time that 2 are water inlet pipe).
In above-mentioned floating stuffing district (the double filtrating area of doing) 6 and 10, be filled with efficient suspension fiber many-sided ball, many-sided ball diameter 2.7cm, proportion approximately 1.007, under the condition of aeration, this filler is in suspension swelling state, strengthen the surface-area of bio-film colonization, can carry out the absorption degradation of pollutent, under the state of aeration not, this filler belongs to the state of static compacting, can be used as filtering layer and filters suspended substance; The effect of above-mentioned aeration tube 4 is that air is inputted to above-mentioned floating stuffing district 6, for the microbial film on filler is built good aerobic environment; The effect of above-mentioned bed course 5 is for carrier filler district provides support, and prevents that filler from being washed away by current; What assembled in above-mentioned excess sludge district 7 comes off microbial film mud by above-mentioned shore pipe 9 dischargers; Water hole 8 is communicated with two reaction chambers, and water hole 8 is provided with the Stainless Steel Wire Mesh of certain pore size, in order to hold back the floating stuffing in above-mentioned floating stuffing district 6 and 10, prevents that the floating stuffing string of two reaction chambers is mixed; The filtering layer that filtrating area 10 utilizes high efficiency filter fiber many-sided ball to pile up and forms filters the sewage after biological membrane biological degraded in floating stuffing district 6, with the suspended substance in trap water and the microbial film coming off.
According to periodic duty: sewage enters reaction chamber bottom by water-in 2, by water distribution system 3 water distribution uniformities, carry out aeration by reaction chamber bottom aerating system 4 simultaneously, the multiaspect fibrous nodules in floating stuffing district (the double filtrating area of doing) 6 suspends and expands, its epontic microbial film carries out biochemical reaction and removes most organic pollutant in sewage, the tiny bubble simultaneously producing when aeration is sheared microbial film aging on filler to come off, the aging microbial film coming off is through entering with the water hole 8 of wire netting the reaction chamber being directly connected with rising pipe 11, now aeration is not carried out in this side reaction chamber, the filler of this reaction chamber filtrating area 10 is in piling up compaction state, current are through out-of-date, filler plays the effect of filtration, filter most suspended substance and the aging microbial film coming off, hold back on the top of reaction chamber and formed the excess sludge district 7 that one deck is made up of the microbial film that comes off simultaneously, get rid of excess sludge by shore pipe 9.Sewage after filtration district 10 filter after by rising pipe 11 qualified discharges.Otherwise in the next cycle, sewage enters reaction chamber by rising pipe (the double water inlet pipe that does) 11, through aeration biochemical reaction and after filtering by water inlet pipe (the double rising pipe that does) 2 discharge systems." aeration-filtration, filtration-aeration " periodically alternate run, can remove the back flushing operation in traditional BAF from this manner, makes water outlet more stable, and denitrogenation dephosphorizing is more abundant.
This device saves the back flushing operation in second pond and the BAF of traditional biological reaction, level of automation is high, facilitate operation maintenance management, water quality after treatment can reach city domestic sewage completely and process one-level A standard, inherit the advantage of traditional technology, overcome again its shortcoming, be obviously better than traditional technology.

Claims (1)

1. an alternative aeration filtering biological reactor, comprise housing, described housing comprises two reaction chambers, it is characterized in that: described two reaction chambers bottom is equipped with intake-outlet, described two reactor top are provided with mud discharging mouth, described two reaction chamber tops are provided with the water hole with metal grill, and described two reaction chamber inner bottom parts are equipped with cloth water gathering system, and described two reaction chambers are upwards aerating system, floating stuffing district and excess sludge district successively.
CN201320515918.0U 2013-08-23 2013-08-23 Alternating aeration filter bioreactor Expired - Fee Related CN203613023U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320515918.0U CN203613023U (en) 2013-08-23 2013-08-23 Alternating aeration filter bioreactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320515918.0U CN203613023U (en) 2013-08-23 2013-08-23 Alternating aeration filter bioreactor

Publications (1)

Publication Number Publication Date
CN203613023U true CN203613023U (en) 2014-05-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320515918.0U Expired - Fee Related CN203613023U (en) 2013-08-23 2013-08-23 Alternating aeration filter bioreactor

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CN (1) CN203613023U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105036332A (en) * 2015-07-10 2015-11-11 南京大学 Alternating internal-recycle biological filter sewage treatment device and method using same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105036332A (en) * 2015-07-10 2015-11-11 南京大学 Alternating internal-recycle biological filter sewage treatment device and method using same

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GR01 Patent grant
C14 Grant of patent or utility model
DD01 Delivery of document by public notice

Addressee: HUBEI PANGU ENVIRONMENTAL PROTECTION ENG.&TECH. CO., LTD.

Document name: Notification that Application Deemed not to be Proposed

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140528

Termination date: 20150823

EXPY Termination of patent right or utility model