CN201896111U - Membrane treatment equipment - Google Patents
Membrane treatment equipment Download PDFInfo
- Publication number
- CN201896111U CN201896111U CN2010205993728U CN201020599372U CN201896111U CN 201896111 U CN201896111 U CN 201896111U CN 2010205993728 U CN2010205993728 U CN 2010205993728U CN 201020599372 U CN201020599372 U CN 201020599372U CN 201896111 U CN201896111 U CN 201896111U
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- Prior art keywords
- pond
- membrane
- treatment facility
- film treatment
- treatment equipment
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Abstract
The utility model discloses membrane treatment equipment, relates to sewage treatment equipment, and aims to provide membrane treatment equipment, wherein service life of membranes is ensured, backwashing and membrane replacing frequency is reduced and operating cost is reduced thereby. The membrane treatment equipment comprises a membrane treatment equipment body, the interior of the membrane treatment equipment body is divided into an anaerobic tank, an anoxic tank and a membrane biological reaction tank by partition boards, seepage holes are arranged at the lower ends of the partition boards, a first air lift backflow device is arranged between the membrane biological reaction tank and the anoxic tank, a second air lift backflow device is arranged between the anoxic tank and the anaerobic tank, a water inlet pipe is arranged in the anaerobic tank, a water outlet pipe is arranged in a biological oxidation tank, and the membrane treatment equipment body is further provided with an equipment compartment. By the aid of advanced treatment of the anaerobic tank and the anoxic tank to sewage, membrane pollution in the membrane biological reaction tank is reduced, sludge load of a membrane biological reactor is reduced, service life of the membranes is ensured, backwashing and membrane replacing frequency is reduced, water outlet effect is guaranteed further, and operating cost is reduced thereby.
Description
Technical field
The utility model relates to a kind of sewage disposal device, relates in particular to a kind of film treatment facility.
Background technology
Existing film treatment facility mainly with membrane bioreactor as the formant in the Sewage treatment systems, if only carry out sewage purification by the effect of membrane bioreactor, can make the sludge loading of membrane bioreactor heavier, cause film to pollute easily, stop up fenestra, make that aeration rate increases, the suction head of pump increases; The increase of the suction head of pump, aeration rate etc. all will cause the increase of running cost; Fenestra stops up the loss that needs frequent cleaning also will increase working cost and manpower and materials; Film work-ing life is short, the diaphragm that needs within a short period of time and more renew, and complicated operation, thus also will increase investment, be unfavorable for Sustainable Development of Enterprises.
The utility model content
At above-mentioned prior art, the technical problems to be solved in the utility model provides a kind of work-ing life that guarantees film, reduces the frequency of back flushing and replacing film, thereby reduces the film treatment facility of working cost.
In order to solve the problems of the technologies described above, the utility model adopts following technical scheme: a kind of film treatment facility, comprise film treatment facility body, described film treatment facility body inner route clapboard separates formation anaerobic pond, anoxic pond, membrane biological reaction pond at interval, the lower end of described dividing plate has the infiltration hole, between membrane biological reaction pond and anoxic pond, be provided with No. 1 gas and carry reflux, be provided with No. 2 gas between anoxic pond and anaerobic pond and carry reflux, be provided with water inlet pipe in the anaerobic pond, be provided with rising pipe in the bio-oxidation pond, this external equipment room that also is provided with of film treatment facility.
As preferably, all hung biologic packing material in described anaerobic pond and the anoxic pond.
As preferably, described membrane biological reaction is provided with film reaction assembly and aeration tube in the pond, and aeration tube is positioned at the gas blower of equipment room by pipe connection.
As preferably, described rising pipe connects the vacuum primingpump that is positioned at equipment room.
As preferably, the corresponding film bio-oxidation pond in the top of described film treatment facility body is provided with manhole.
Compared with prior art, the utlity model has following advantage: because process anaerobic pond and anoxic pond are to the processing formerly of sewage, make the film in the film bio-oxidation pond pollute reduction, reduce the sludge loading of membrane bioreactor, reduce the suction head and the aeration rate of pump, guarantee the work-ing life of film simultaneously, reduce the frequency of back flushing and replacing film, and can guarantee good water outlet effect, thereby reduce working cost.
Description of drawings
Fig. 1 is the structural representation of the utility model embodiment.
Embodiment
The utility model will be further described below in conjunction with drawings and Examples.
Referring to Fig. 1, a kind of film treatment facility, comprise film treatment facility body, described film treatment facility body inner route clapboard 4 separates formation anaerobic pond 1 at interval, anoxic pond 2, membrane biological reaction pond 3, described film treatment facility body is made into integration by steel, dividing plate 4 also is a steel plate, have the infiltration hole in the lower end of dividing plate 4, be provided with No. 1 gas in membrane biological reaction pond 3 and 2 of anoxic pond and carry reflux 7,1 of anoxic pond 2 and anaerobic pond are provided with No. 2 gas and carry reflux 8, have all hung biologic packing material 5 in described anaerobic pond 1 and the anoxic pond 2, are provided with water inlet pipe 6 in the anaerobic pond 1, be provided with rising pipe 13 in the bio-oxidation pond 3, this external equipment room 9 that also is provided with of film treatment facility; Be provided with film reaction assembly 10 and aeration tube 11 in the described membrane biological reaction pond 3, aeration tube 11 is positioned at the below of film reaction assembly 10, and aeration tube 11 is positioned at the gas blower 12 of equipment room 9 by pipe connection; Described rising pipe 13 connects the vacuum primingpump 14 that is positioned at equipment room 9, and the corresponding film bio-oxidation pond 3 in the top of described film treatment facility body is provided with manhole 15.
During the utility model work, sewage at first promotes the anaerobic pond 1 that enters film treatment facility body by pump by water inlet pipe 6, is provided with biologic packing material 5 in the anaerobic pond 1, and the water after anaerobic treatment flows automatically respectively and enters anoxic pond 2, membrane biological reaction pond 3; Be provided with biologic packing material in the anoxic pond 2, film reaction assembly 10 in submergence in the membrane biological reaction pond 3, is oxygenation in the membrane biological reaction pond 3 by gas blower 12 and aeration tube 11; Sewage can directly be discharged by rising pipe 13 sucking-offs by vacuum primingpump 14 after handle in membrane biological reaction pond 3, but also reuse, 2 of membrane biological reaction pond 3 and anoxic pond are provided with No. 1 gas and carry reflux 7, can allow mixed-liquor return to anoxic pond 2, to reach the purpose of denitrogenation; 1 of anoxic pond 2 and anaerobic pond are provided with No. 2 gas and carry reflux, and anoxic pond 2 part mud are back to anaerobic pond 1 to replenish the sludge concentration of anaerobic pond 1, make treatment effect better; This film treatment facility can be used for sanitary sewage disposal, Hospital Sewage Treatment, wastewater from car washer reuse etc.
Claims (5)
1. film treatment facility, it is characterized in that: comprise film treatment facility body, described film treatment facility body inner route clapboard (4) separates formation anaerobic pond (1) at interval, anoxic pond (2), membrane biological reaction pond (3), the lower end of described dividing plate (4) has the infiltration hole, between membrane biological reaction pond (3) and anoxic pond (2), be provided with No. 1 gas and carry reflux (7), be provided with No. 2 gas between anoxic pond (2) and anaerobic pond (1) and carry reflux (8), be provided with water inlet pipe (6) in the anaerobic pond (1), be provided with rising pipe (13) in the bio-oxidation pond (3), this external equipment room (9) that also is provided with of film treatment facility.
2. according to claim a kind of film treatment facility is characterized in that: all hung biologic packing material (5) in described anaerobic pond (1) and the anoxic pond (2).
3. a kind of film treatment facility according to claim 1 is characterized in that: be provided with film reaction assembly (10) and aeration tube (sheet) in the described membrane biological reaction pond (3), aeration tube (11) is positioned at the gas blower (12) of equipment room (9) by pipe connection.
4. a kind of film treatment facility according to claim 1 is characterized in that: described rising pipe (13) is connected with the vacuum primingpump (14) that is positioned at equipment room (9).
5. a kind of film treatment facility according to claim 1 is characterized in that: the corresponding film bio-oxidation pond in the top of described film treatment facility body (3) is provided with hand-hole (15).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010205993728U CN201896111U (en) | 2010-11-10 | 2010-11-10 | Membrane treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010205993728U CN201896111U (en) | 2010-11-10 | 2010-11-10 | Membrane treatment equipment |
Publications (1)
Publication Number | Publication Date |
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CN201896111U true CN201896111U (en) | 2011-07-13 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2010205993728U Expired - Fee Related CN201896111U (en) | 2010-11-10 | 2010-11-10 | Membrane treatment equipment |
Country Status (1)
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CN (1) | CN201896111U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104843867A (en) * | 2015-05-19 | 2015-08-19 | 新乡市蓝海环境工程有限公司 | Membrane biological wastewater treatment device |
CN105502857A (en) * | 2016-02-17 | 2016-04-20 | 王纬 | Sewage treatment equipment |
CN106927561A (en) * | 2016-11-21 | 2017-07-07 | 江西博鑫精陶环保科技有限公司 | A kind of method and apparatus of use inoranic membrane, filler and liquid integrated treatment sewage |
CN111003807A (en) * | 2019-12-25 | 2020-04-14 | 江苏清泉环保集团有限公司 | Labyrinth type integrated MBR (membrane bioreactor) |
-
2010
- 2010-11-10 CN CN2010205993728U patent/CN201896111U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104843867A (en) * | 2015-05-19 | 2015-08-19 | 新乡市蓝海环境工程有限公司 | Membrane biological wastewater treatment device |
CN105502857A (en) * | 2016-02-17 | 2016-04-20 | 王纬 | Sewage treatment equipment |
CN106927561A (en) * | 2016-11-21 | 2017-07-07 | 江西博鑫精陶环保科技有限公司 | A kind of method and apparatus of use inoranic membrane, filler and liquid integrated treatment sewage |
CN111003807A (en) * | 2019-12-25 | 2020-04-14 | 江苏清泉环保集团有限公司 | Labyrinth type integrated MBR (membrane bioreactor) |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110713 Termination date: 20151110 |
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EXPY | Termination of patent right or utility model |