CN201330194Y - Assemble-type three-phase separator for anaerobic reactor - Google Patents
Assemble-type three-phase separator for anaerobic reactor Download PDFInfo
- Publication number
- CN201330194Y CN201330194Y CNU2009201054268U CN200920105426U CN201330194Y CN 201330194 Y CN201330194 Y CN 201330194Y CN U2009201054268 U CNU2009201054268 U CN U2009201054268U CN 200920105426 U CN200920105426 U CN 200920105426U CN 201330194 Y CN201330194 Y CN 201330194Y
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- collection chamber
- collecting chamber
- anaerobic reactor
- gas collecting
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Abstract
The utility model discloses an assemble-type three-phase separator for an anaerobic reactor, comprising a gas collector, a sealing plate and a drain tank. There are multiple gas collectors, each of which comprises a primary gas collecting chamber and an auxiliary gas collecting chamber; the auxiliary gas collecting chamber is arranged on the primary gas collecting chamber which is connected with the primary gas collecting chamber through a connecting hole; each of the gas collectors comprises a sealing plate which is arranged at one end of the auxiliary gas collecting chamber; the drain tank is arranged above the primary gas collecting chamber and is arranged parallel to the primary gas collecting chamber. The separator of the utility model is simple to produce, has low cost, is suitable for modularized production and scene assembling, is durable and has high separation efficiency.
Description
Technical field
The utility model relates to a kind of triphase separator, relates in particular to the gas, liquid, solid triphase separator in a kind of anerobic sowage treatment unit.
Background technology
At present, sewage disposal technology commonly used is divided into materialization processing and biological treatment, and the materialization treatment process only uses as pretreatment technology, and its processing cost is very high, and biological treatment is divided into anaerobic and aerobic two classes.The recognized technology that Anaerobic Microbiological Treatment Technology is handled as high concentrated organic wastewater has been widely applied to many industries such as papermaking, pharmacy, printing and dyeing, food, has obtained good effect.Wherein using maximum is exactly up flow anaerobic sludge blanket reactor.
Up flow anaerobic sludge blanket reactor is collection biological respinses and is deposited in one in constructional characteristics, is a kind of anaerobic reactor of compact construction, mainly contains following a few part and forms:
1, water distribution system
Sewage at first is assigned on the cross section of whole reactor uniformly by the water distribution system at the bottom of the pond, in uniform water distribution, has also played the effect that waterpower stirs.
2, reaction zone
Reaction zone is the main position of upflow anaerobic sludge blanket process, comprises granule sludge district and suspended sludge area.Stayed a large amount of anaerobic sludges at the reaction zone internal memory, the mud with good cohesion and sedimentation function is with after sewage contacts, and organic pollutant is by mass consumption, simultaneously self continuous increment.Microorganism in the mud also in decomposing organic matter, has also produced a lot of small biogas bubbles, and these bubbles constantly merge in the process that rises, and form than air pocket gradually.
3, triphase separator
Form by settling region, backflow seam and sealing gland.Its function is that gas (biogas), solid (mud) and liquid (waste water) three-phase are separated.Biogas enters air chamber, and mud precipitates in the settling region, and is back to reaction zone through the seam that refluxes.After the precipitation clarification, waste water is discharged reactor by the drainage tray on reactor top.
At present, triphase separator is generally integrated apparatus, and installation difficulty is big, and construction quality can not finely guarantee, the movement requirement height, and cost is also higher.In addition, general triphase separator all exists separation efficiency low, often leaks air or runs the mud phenomenon, is unfavorable for the steady running and the maintenance of anaerobic reactor.
Summary of the invention
For solving problem and the defective that incorporate three phase separation apparatus exists, the utility model provides a kind of triphase separator of modular on-site consolidation, this triphase separator is installed simple, convenient transportation, gas, solid, liquid separating effect have been improved, effectively guarantee the steady running of anaerobic reactor, reduced cost and installation and transportation cost simultaneously.
The utility model is achieved through the following technical solutions:
A kind of piecing assembly triphase separator that is used for anaerobic reactor that the utility model is related comprises:
Gas extractor, sealing plate and drainage tray, described gas extractor is set to a plurality of, and each gas extractor comprises main collection chamber and secondary collection chamber, and secondary collection chamber is arranged on the main collection chamber; Comprise a sealing plate in described each gas extractor, and the sealing plate is arranged on an end of secondary collection chamber.
Comprise a main collection chamber and four or more secondary collection chamber in described each gas extractor.
Described secondary collection chamber is made of two blocks of polypropylene PP plates, and the angle between two blocks of polypropylene PP plates is 80 °.
Also comprise a drainage tray in described each gas extractor, this drainage tray is arranged at the top of main collection chamber, and is arranged in parallel with main collection chamber.
Described secondary collection chamber comprises secondary collection chamber and following secondary collection chamber, and is respectively arranged with communicating aperture in the secondary up and down collection chamber.
The beneficial effect of the technical scheme that the utility model provides is:
1, but each module standardized designs all is suitable for on-site consolidation, and can guarantees setting accuracy;
2, main material is corrosion resistant plastic plate, can guarantee the anaerobic reactor long-time steady operation;
3, manufacturing and installation cost are low, can reduce construction costs about 10%;
4, material is light, and mounting means is flexible, and maintenance and replacing are convenient;
5, gas, solid, liquid separating power have efficiently been kept the high sludge concentration and the high throughput of reactor.
Description of drawings
Fig. 1 is an orthographic plan of the present utility model;
Fig. 2 is a sectional view of the present utility model;
Fig. 3 is another sectional view of the present utility model;
Fig. 4 is a secondary collection chamber sectional view of the present utility model.
Embodiment
For making the purpose of this utility model, technical scheme and advantage clearer, the utility model embodiment is described in further detail below in conjunction with accompanying drawing:
As Fig. 1, Fig. 2, Fig. 3, shown in Figure 4, showed plane of the present utility model and cross-section structure, this structure comprises gas extractor, sealing plate 4 and drainage tray 8, and described gas extractor is a plurality of, each gas extractor comprises main collection chamber 1 and secondary collection chamber, and secondary collection chamber is arranged on the main collection chamber 1; Be provided with a sealing plate 4 in described each gas extractor.Described secondary collection chamber comprises secondary collection chamber 6 and secondary collection chamber 7 down, and goes up secondary collection chamber 6 and be respectively arranged with communicating aperture 5 in the secondary collection chamber 7 down, and secondary collection chamber is made of two blocks of polypropylene PP plates 2, and the angle between two polypropylene PP swash plates 2 is 80 °.One end of described secondary collection chamber is a sealing plate 4, and the communicating aperture 5 of biogas from secondary collection chamber enters in the main collection chamber 1.The top of main collection chamber 1 connects biogas arm 3, and all biogas arms are connected to a biogas and are responsible for, and send anaerobic reactor.Each anaerobic reactor adopts stdn to make, and each anaerobic reactor has 2 groups of triphase separators at least according to size.Also comprise a drainage tray 8 in described each gas extractor, this drainage tray 8 is arranged at the top of main collection chamber 1, and is arranged in parallel with main collection chamber 1.
Anaerobic reactor is in operational process, and the gas of generation, solid, liquid three-phase mixture enter triphase separator from the bottom to top, and what at first enter is first step three phase separation unit, comprises secondary collection chamber 7, polypropylene PP plate 2, communicating aperture 5 down.Sewage is slowly risen by the intermediate reflux slit of two collection chambers, sludge settling in the water is to polypropylene PP swash plate 2, glide gradually along polypropylene PP swash plate 2 then, seam is back to sludge blanket by refluxing, tiny biogas bubble near vertical in the water rises to down secondary collection chamber 7, converge the back and enter main collection chamber 1, be delivered to outside the reactor by biogas pipeline at last by communicating aperture 5.After first step three phase separation, small bubbles rise to secondary three phase separation unit together with a small part mud with sewage in the mixed solution, and its two-stage three phase separation principle is identical.After the two-stage three phase separation, water outlet is discharged anaerobic reactor by the drainage tray on main collection chamber 1 top, biogas is discharged reactor by the biogas pipeline that is communicated with main collection chamber 1, mud is after converge the negative area, precipitate by self gravitation, get back to sludge blanket and participate in reaction again, effectively guaranteed the sludge concentration and the processing efficiency of anaerobic reaction.
The above; it only is the preferable embodiment of the utility model; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; the variation that can expect easily or replacement all should be encompassed within the protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of claim.
Claims (5)
1, the piecing assembly triphase separator that is used for anaerobic reactor, comprise gas extractor, sealing plate and drainage tray, it is characterized in that described gas extractor is set to a plurality of, each gas extractor comprises main collection chamber and secondary collection chamber, and secondary collection chamber is arranged on the main collection chamber; Comprise a sealing plate in described each gas extractor, and the sealing plate is arranged on an end of secondary collection chamber.
2, the piecing assembly triphase separator that is used for anaerobic reactor according to claim 1 is characterized in that, comprises a main collection chamber and four or more secondary collection chamber in described each gas extractor.
3, the piecing assembly triphase separator that is used for anaerobic reactor according to claim 1 and 2 is characterized in that, described secondary collection chamber is made of two blocks of polypropylene PP plates, and the angle between two blocks of polypropylene PP plates is 80 °.
4, the piecing assembly triphase separator that is used for anaerobic reactor according to claim 1 is characterized in that, also comprises a drainage tray in described each gas extractor, and this drainage tray is arranged at the top of main collection chamber, and is arranged in parallel with main collection chamber.
5, the piecing assembly triphase separator that is used for anaerobic reactor according to claim 1 is characterized in that, described main collection chamber and drainage tray are arranged apart; Described secondary collection chamber comprises secondary collection chamber and following secondary collection chamber, and is respectively arranged with communicating aperture in the secondary up and down collection chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009201054268U CN201330194Y (en) | 2009-01-23 | 2009-01-23 | Assemble-type three-phase separator for anaerobic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2009201054268U CN201330194Y (en) | 2009-01-23 | 2009-01-23 | Assemble-type three-phase separator for anaerobic reactor |
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| Publication Number | Publication Date |
|---|---|
| CN201330194Y true CN201330194Y (en) | 2009-10-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNU2009201054268U Expired - Fee Related CN201330194Y (en) | 2009-01-23 | 2009-01-23 | Assemble-type three-phase separator for anaerobic reactor |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102241433A (en) * | 2010-05-11 | 2011-11-16 | 泰州康泰环保科技有限公司 | Efficient combined three-phase separator |
| CN103332785A (en) * | 2013-07-03 | 2013-10-02 | 刘锋 | Combined three-phase separation device for efficient anaerobic reactor |
-
2009
- 2009-01-23 CN CNU2009201054268U patent/CN201330194Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102241433A (en) * | 2010-05-11 | 2011-11-16 | 泰州康泰环保科技有限公司 | Efficient combined three-phase separator |
| CN103332785A (en) * | 2013-07-03 | 2013-10-02 | 刘锋 | Combined three-phase separation device for efficient anaerobic reactor |
| CN103332785B (en) * | 2013-07-03 | 2016-01-20 | 刘锋 | A kind of Combined three phase tripping device for high efficiency anaerobic reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHANG YAJUN Free format text: FORMER OWNER: BEIJING JIYATE ENVIRONMENTAL ENGINEERING CO., LTD. Effective date: 20130621 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 101400 HUAIROU, BEIJING TO: 100085 HAIDIAN, BEIJING |
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| TR01 | Transfer of patent right |
Effective date of registration: 20130621 Address after: 100085 Beijing city Haidian District East Road No. 1, block E 401-A a power surplus Patentee after: Zhang Yajun Address before: Seven in 101400 districts in Beijing District of Huairou Yanqi Industrial Development Zone No. 36 Patentee before: Beijing Jiyate Environmental Engineering Co., LTD. |
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| ASS | Succession or assignment of patent right |
Owner name: BEIJING JIYATE ENVIRONMENTAL ENGINEERING CO., LTD. Free format text: FORMER OWNER: ZHANG YAJUN Effective date: 20130917 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 100085 HAIDIAN, BEIJING TO: 101400 HUAIROU, BEIJING |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130917 Address after: Seven in 101400 districts in Beijing District of Huairou Yanqi Industrial Development Zone No. 36 Patentee after: Beijing Jiyate Environmental Engineering Co., LTD. Address before: 100085 Beijing city Haidian District East Road No. 1, block E 401-A a power surplus Patentee before: Zhang Yajun |
|
| C56 | Change in the name or address of the patentee |
Owner name: BEIJING G + T ENVIRONMENTAL PROTECTION TECHNOLOGY Free format text: FORMER NAME: BEIJING JIYATE ENVIRONMENTAL ENGINEERING CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: Seven in 101400 districts in Beijing District of Huairou Yanqi Industrial Development Zone No. 36 Patentee after: BEIJING G&T ENVIRONMENTAL PROTECTION SCIENCE AND TECHNOLOGY CO., LTD. Address before: Seven in 101400 districts in Beijing District of Huairou Yanqi Industrial Development Zone No. 36 Patentee before: Beijing Jiyate Environmental Engineering Co., LTD. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20091021 Termination date: 20170123 |
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| CF01 | Termination of patent right due to non-payment of annual fee |