CN205011466U - Anaerobic reactor - Google Patents
Anaerobic reactor Download PDFInfo
- Publication number
- CN205011466U CN205011466U CN201520652521.5U CN201520652521U CN205011466U CN 205011466 U CN205011466 U CN 205011466U CN 201520652521 U CN201520652521 U CN 201520652521U CN 205011466 U CN205011466 U CN 205011466U
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- phase separator
- housing
- anaerobic reactor
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- model
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Abstract
The utility model relates to an anaerobic reactor, include: casing and water -locator, the casing lower extreme has cup jointed the tower tray, the water -locator lower extreme is connected with the sewage inlet tube, it is overhanging that the sewage inlet tube passes the tower tray port, the fixed one -level three -phase separator that is provided with in tower tray upper end, be the fluidized bed reaction room between water -locator and the one -level three -phase separator, the fixed second grade three -phase separator that is provided with in one -level three -phase separator top, be degree of depth evolution reacting chamber between one -level three -phase separator and the second grade three -phase separator, second grade three -phase separator upper end is provided with whirl vapour and liquid separator, whirl vapour and liquid separator upper end is provided with the marsh gas outlet pipe, whirl vapour and liquid separator right side is provided with the clear water outlet pipe, the utility model discloses equipment is simple, and the operation is convenient, need not establish sedimentation tank and return sludge device, need not fill the filler, does not also need to establish the mechanical stirring device in the reaction zone, and the cost is relatively low, the management of being convenient for, and do not have the jam problem.
Description
Technical field
The utility model relates to field of sewage treatment equipment, specifically a kind of anaerobic reactor.
Background technology
Along with the reach of science, deepening continuously of scientific research, many new technologies, novel material, new concept is widely used in environment protection industry, makes the significant progress that China environmental protection technology obtains.The industries such as food, biology, chemical industry are discharged most of waste water and are all belonged to high concentrated organic wastewater, and materialization, the biochemical treatment difficulty of utilization routine reach processing intent, and there is operational administrative, investment is large, the high system problem of running cost simultaneously.Anaerobic fluidized bed reactor is a kind of biomembrance process treatment process efficiently.It utilizes the material of the high surface areas such as sand for carrier.Anaerobion on the surface of sand or other carrier, becomes flow state with form membrane knot in sewage, and the organism in microorganism and sewage carries out Contact-sorption decomposing organic matter, thus reaches the object of process.The existing anaerobic reactor water distribution mouth of pipe easily blocks, and usually occurs that water conservancy stirs uneven, the short flow phenomenon of Sludge Bed, needs to improve.
Based on above reason, needing a kind of anaerobic reactor to be devised, by arranging vortex layer in enclosure interior, effectively making sewage and mud fully mix; By arranging agitator, mixture constantly being stirred, making the abundant contact reacts of mixture; By arranging three phase separation, the gas that effective separating reaction produces, water and mud, the circulation of the collection and reaction of being convenient to gas is carried out; By arranging drainage layer, secondary filtration can be carried out to clear water, improving the purity of clear water, i.e. a kind of anaerobic reactor.
Utility model content
In order to solve the technical problem that above-mentioned existing anaerobic reactor exists, the utility model provides a kind of anaerobic reactor.
The utility model solves the technical scheme that its technical problem adopts:
A kind of anaerobic reactor, comprising: housing and skirt, inside, described housing lower end is provided with vortex layer, and described housing bottom is connected with wastewater inlet pipeline; Described vortex layer upper end is provided with agitator, and described agitator is fixedly connected with housing by gusset; Housing central section is provided with mud inlet ductwork, is provided with triphase separator above housing, and triphase separator is connected with drainage layer; Described drainage layer lower end is provided with clear water output; Described triphase separator upper end is provided with gas outlet tube; Described housing and skirt are welded to connect.
As preferred version of the present utility model, be evenly equipped with bolt hole around described skirt, described skirt adopts carbon steel material to make, and while proof strength, saves cost of manufacture.
As preferred version of the present utility model, described housing lower end is set to round-corner transition structure, the concentrated stress that effective abatement apparatus in use produces.
As preferred version of the present utility model, described drainage layer adopts biofilm structure, effectively filters microorganism in clear water.
The beneficial effects of the utility model are: a kind of anaerobic reactor, by arranging vortex layer in enclosure interior, effectively make sewage and mud fully mix; By arranging agitator, mixture constantly being stirred, making the abundant contact reacts of mixture; By arranging three phase separation, the gas that effective separating reaction produces, water and mud, the circulation of the collection and reaction of being convenient to gas is carried out; By arranging drainage layer, secondary filtration can be carried out to clear water, improving the purity of clear water; The utility model equipment is simple, and it is convenient to run, and cost is relatively low, is convenient to management, and there is not blockage problem.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is structural representation of the present utility model.
In figure: 1, housing, 2, vortex layer, 3, triphase separator, 4, drainage layer, 5, agitator, 6, gusset, 7, mud inlet ductwork, 8, clear water output, 9, gas outlet tube, 10, skirt, 11, wastewater inlet pipeline.
Embodiment
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
As shown in Figure 1, a kind of anaerobic reactor described in the utility model, comprising: housing 1 and skirt 10, and inside, described housing 1 lower end is provided with vortex layer 2, and described housing 1 bottom is connected with wastewater inlet pipeline 11; Described vortex layer 2 upper end is provided with agitator 5, and described agitator 5 is fixedly connected with housing 1 by gusset 6; Be provided with mud inlet ductwork 7 in the middle part of housing 1, be provided with triphase separator 3 above housing 1, triphase separator 3 is connected with drainage layer 4; Described drainage layer 4 lower end is provided with clear water output 8; Described triphase separator 3 upper end is provided with gas outlet tube 9; Described housing 1 and skirt 10 are welded to connect; Be evenly equipped with bolt hole around described skirt 10, described skirt 10 adopts carbon steel material to make, and while proof strength, saves cost of manufacture; Described housing 1 lower end is set to round-corner transition structure, the concentrated stress that effective abatement apparatus in use produces; Described drainage layer 4 adopts biofilm structure, effectively filters microorganism in clear water.
More than show and describe ultimate principle of the present utility model, principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (5)
1. an anaerobic reactor, comprise: housing (1) and skirt (10), it is characterized in that: described housing (1) inside, lower end is provided with vortex layer (2), described housing (1) bottom is connected with wastewater inlet pipeline (11); Described vortex layer (2) upper end is provided with agitator (5), and described agitator (5) is fixedly connected with housing (1) by gusset (6); Housing (1) middle part is provided with mud inlet ductwork (7), and housing (1) top is provided with triphase separator (3), and triphase separator (3) is connected with drainage layer (4); Described drainage layer (4) lower end is provided with clear water output (8); Described triphase separator (3) upper end is provided with gas outlet tube (9).
2. a kind of anaerobic reactor according to claim 1, is characterized in that: described skirt (10) is evenly equipped with bolt hole around, and described skirt (10) adopts carbon steel material to make.
3. a kind of anaerobic reactor according to claim 1, is characterized in that: described housing (1) lower end is set to round-corner transition structure.
4. a kind of anaerobic reactor according to claim 1, is characterized in that: described drainage layer (4) adopts biofilm structure.
5. a kind of anaerobic reactor according to claim 1, is characterized in that: described housing (1) and skirt (10) are welded to connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520652521.5U CN205011466U (en) | 2015-08-26 | 2015-08-26 | Anaerobic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520652521.5U CN205011466U (en) | 2015-08-26 | 2015-08-26 | Anaerobic reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205011466U true CN205011466U (en) | 2016-02-03 |
Family
ID=55210080
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520652521.5U Expired - Fee Related CN205011466U (en) | 2015-08-26 | 2015-08-26 | Anaerobic reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205011466U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101938174B1 (en) | 2017-03-24 | 2019-01-14 | 대우조선해양 주식회사 | Three Phase Separator and Boil-Off Gas Re-liquefaction System |
-
2015
- 2015-08-26 CN CN201520652521.5U patent/CN205011466U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101938174B1 (en) | 2017-03-24 | 2019-01-14 | 대우조선해양 주식회사 | Three Phase Separator and Boil-Off Gas Re-liquefaction System |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160203 Termination date: 20170826 |