CN209906436U - Good three-phase separator who is used for anaerobic tower of stability - Google Patents
Good three-phase separator who is used for anaerobic tower of stability Download PDFInfo
- Publication number
- CN209906436U CN209906436U CN201920054281.7U CN201920054281U CN209906436U CN 209906436 U CN209906436 U CN 209906436U CN 201920054281 U CN201920054281 U CN 201920054281U CN 209906436 U CN209906436 U CN 209906436U
- Authority
- CN
- China
- Prior art keywords
- phase separator
- separator device
- pipe
- gas
- water
- 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.)
- Active
Links
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a good three-phase separator who is used for anaerobic tower of stability, comprising a base plate, the bottom plate top is equipped with the casing, be equipped with three-phase separator device in the casing, three-phase separator device includes a plurality of gas collecting channel, be equipped with the through-hole on the gas collecting channel, it is equipped with the passageway to connect between the gas collecting channel, three-phase separator device bottom is connected and is equipped with the inner loop back flow, three-phase separator device top is connected and is equipped with the pipeline, the pipeline is kept away from three-phase separator device one end is connected with catch water, the casing top is equipped with the platform, catch water places on the platform, catch water's top is equipped with the marsh gas pipe, catch water one side is equipped with the inner loop tedge, the inner loop tedge run through in three-phase separator device. Has the advantages that: the separated gas is discharged from the methane pipe, and the wastewater enters the bottom of the reactor shell along the internal circulation return pipe to complete internal circulation.
Description
Technical Field
The utility model relates to a three-phase separator particularly, relates to a good three-phase separator who is used for anaerobic tower of stability.
Background
CN201220370033.1 discloses a three-phase separator, including establishing the opening in three-phase separator lower part, the oblique top of open-ended is equipped with the refraction board of slope, the both ends of refraction board are connected with the baffle, and three-phase separator top is equipped with the roof of connecting refraction board and baffle, is equipped with the gas collecting pipe that communicates the inside to anaerobic reactor top collecting space of three-phase separator on the roof. By adopting the scheme, when solid, liquid and gas are separated in the methane generation process, the auxiliary of related filler substances with special physical and chemical properties is not needed, the structure is simple and effective, the maintenance is convenient, the maintenance cost is low, the separation is completed through physical collision, and the separation effect is good. However, the three-phase separator in the above patent cannot ensure stable discharge of gas, thereby affecting the effect of wastewater treatment.
An effective solution to the problems in the related art has not been proposed yet.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a stability is good is used for anaerobic tower's three-phase separator to solve the problem that proposes in the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme: a three-phase separator with good stability for an anaerobic tower comprises a bottom plate, wherein a shell is arranged above the bottom plate, a three-phase separator device is arranged in the shell and comprises a plurality of gas collecting hoods, through holes are formed in the gas collecting hoods, channels are connected among the gas collecting hoods, an internal circulation backflow pipe is connected to the bottom of the three-phase separator device, a pipeline is connected to the top of the three-phase separator device, one end, away from the pipeline, of the three-phase separator device is connected with a steam-water separator, a platform is arranged at the top of the shell, the steam-water separator is placed on the platform, a biogas pipe is arranged at the top of the steam-water separator, an internal circulation ascending pipe is arranged on one side of the steam-water separator and penetrates through the three-phase separator device, a water collecting tank is arranged at the top in the shell and is connected with a water outlet pipe, an external circulation pipe penetrates through the shell, valves are arranged on the external circulation pipe and the water outlet pipe, the external circulation pipe is located below the three-phase separator device, and a sampling pipe is arranged below the external circulation pipe.
Furthermore, the included angle of the gas collecting hood is 60 degrees.
Further, the distance between the gas collecting hoods is 0.2 m.
Furthermore, the opening of the gas collecting hood is 0.4 meter.
Further, the number of the steam-water separators is two.
Furthermore, the top of the three-phase separator device is provided with a first three-phase separator pressing beam, the bottom of the three-phase separator device is provided with a second three-phase separator pressing beam, and the second three-phase separator pressing beam is far away from one side of the three-phase separator device which is symmetrically provided with a three-phase separator bearing beam.
The utility model provides a stability is good is used for anaerobic tower's three-phase separator, beneficial effect as follows:
(1) the three-phase separator device is arranged in the shell to carry out multi-layer separation, so that sewage is treated, three substances of liquid, water and solid of the anaerobic tower are separated, the liquid rises through the internal circulation ascending pipe, the pollution falls, partial waste water under the action of gas enters the steam-water separator, the separated gas is discharged from the biogas pipe, and the waste water enters the bottom of the reactor shell along the internal circulation return pipe and then completes internal circulation.
(2) The included angle of the gas-collecting hood is set to be 60 degrees, and the opening of the gas-collecting hood from the other angle is 0.4 meter, so that the full solid-liquid separation and the stable discharge of gas are ensured; the distance between every two gas-collecting hoods is 0.2 m, so that stable upward flow is ensured.
(3) The three-phase separator pressing beam I and the three-phase separator pressing beam II are arranged, so that the three-phase separator device is fixedly supported. Through being equipped with the three-phase separator spandrel girder to play fine bearing effect, improved the stability of three-phase separator device.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required to be used in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
FIG. 1 is a schematic structural diagram of a three-phase separator for an anaerobic tower with good stability according to an embodiment of the present invention;
fig. 2 is a schematic structural diagram of a three-phase separator device with good stability in a three-phase separator for an anaerobic tower according to an embodiment of the present invention.
Reference numerals:
1. a base plate; 2. a housing; 3. a three-phase separator device; 4. a gas-collecting hood; 5. a through hole; 6. a channel; 7. an internal circulation return pipe; 8. a pipeline; 9. a steam-water separator; 10. a platform; 11. a biogas pipe; 12. an internal circulation riser pipe; 13. a water collection tank; 14. a water outlet pipe; 15. an external circulation pipe; 16. a sampling tube; 17. pressing a beam II of the three-phase separator; 18. a first three-phase separator pressing beam; 19. a three-phase separator spandrel girder; 20. and (4) a valve.
Detailed Description
The following, with reference to the drawings and the detailed description, further description of the present invention is made:
the first embodiment is as follows:
referring to fig. 1-2, a three-phase separator for an anaerobic tower with good stability according to an embodiment of the present invention includes a bottom plate 1, a housing 2 is disposed above the bottom plate 1, a three-phase separator device 3 is disposed in the housing 2, the three-phase separator device 3 includes a plurality of gas collecting hoods 4, through holes 5 are disposed on the gas collecting hoods 4, a channel 6 is disposed between the gas collecting hoods 4, an internal circulation return pipe 7 is disposed at the bottom of the three-phase separator device 3, a pipe 8 is disposed at the top of the three-phase separator device 3, one end of the pipe 8 away from the three-phase separator device 3 is connected to a steam-water separator 9, a platform 10 is disposed at the top of the housing 2, the steam-water separator 9 is disposed on the platform 10, a biogas pipe 11 is disposed at the top of the steam-water separator 9, an internal circulation riser 12 is disposed at one side of the steam-water separator, the internal circulation ascending pipe 12 penetrates through the three-phase separator device 3, a water collecting tank 13 is arranged at the top in the shell 2, the water collecting tank 13 is connected with a water outlet pipe 14, an external circulation pipe 15 penetrates through the shell 2, valves 20 are arranged on the external circulation pipe 15 and the water outlet pipe 14, the external circulation pipe 15 is located below the three-phase separator device 3, and a sampling pipe 16 is arranged below the external circulation pipe 15.
Through the above technical scheme of the utility model, beneficial effect: the three-phase separator device 3 is arranged in the shell 2 to carry out multi-layer separation, so that sewage is treated, three substances of liquid, water and solid of the anaerobic tower are separated, the liquid rises through the internal circulation ascending pipe 12, pollution is reduced, partial waste water under the action of gas enters the steam-water separator 9, the separated gas is discharged from the methane pipe 11, and the waste water enters the bottom of the reactor shell 2 along the internal circulation return pipe 7 to complete internal circulation.
Example two:
referring to fig. 1 and 2, for the gas collecting channel 4, the included angle of the gas collecting channel 4 is 60 degrees. For the gas collecting channels 4, the spacing between the gas collecting channels 4 is 0.2 m. For the gas collecting channel, the opening of the gas collecting channel 4 is 0.4 meter. For the steam-water separator 9, the number of the steam-water separator 9 is two.
Through the above technical scheme of the utility model, beneficial effect: the included angle of the gas-collecting hood 4 is set to be 60 degrees, and the opening of the gas-collecting hood 4 from the other angle is 0.4 meter, so that the full solid-liquid separation and the stable discharge of gas are ensured; the distance between each gas-collecting channel 4 is 0.2 m, so that a stable upward flow is ensured.
Example three:
referring to fig. 1, for the three-phase separator device 3, a first three-phase separator pressing beam 18 is disposed at the top of the three-phase separator device 3, a second three-phase separator pressing beam 17 is disposed at the bottom of the three-phase separator device 3, and a third three-phase separator bearing beam 19 is symmetrically disposed on a side of the second three-phase separator pressing beam 17 away from the three-phase separator device 3.
Through the above technical scheme of the utility model, beneficial effect: the three-phase separator device 3 is fixedly supported by the three-phase separator pressing beam I18 and the three-phase separator pressing beam II 17. By arranging the three-phase separator bearing beam 19, a good bearing effect is achieved, and the stability of the three-phase separator device 3 is improved.
To sum up, with the aid of the above technical scheme of the utility model, theory of operation and all beneficial effects: the three-phase separator device 3 is arranged in the shell 2 to carry out multi-layer separation, so that sewage is treated, three substances of liquid, water and solid of the anaerobic tower are separated, the liquid rises through the internal circulation ascending pipe 12, pollution is reduced, partial waste water under the action of gas enters the steam-water separator 9, the separated gas is discharged from the methane pipe 11, and the waste water enters the bottom of the reactor shell 2 along the internal circulation return pipe 7 to complete internal circulation. The included angle of the gas-collecting hood 4 is set to be 60 degrees, and the opening of the gas-collecting hood 4 from the other angle is 0.4 meter, so that the full solid-liquid separation and the stable discharge of gas are ensured; the distance between each gas-collecting channel 4 is 0.2 m, so that a stable upward flow is ensured. The three-phase separator device 3 is fixedly supported by the three-phase separator pressing beam I18 and the three-phase separator pressing beam II 17. By arranging the three-phase separator bearing beam 19, a good bearing effect is achieved, and the stability of the three-phase separator device 3 is improved.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The three-phase separator with good stability for the anaerobic tower is characterized by comprising a bottom plate (1), a shell (2) is arranged above the bottom plate (1), a three-phase separator device (3) is arranged in the shell (2), the three-phase separator device (3) comprises a plurality of gas collecting hoods (4), through holes (5) are formed in the gas collecting hoods (4), a channel (6) is connected between the gas collecting hoods (4), an internal circulation return pipe (7) is connected to the bottom of the three-phase separator device (3), a pipeline (8) is connected to the top of the three-phase separator device (3), one end, far away from the three-phase separator device (3), of the pipeline (8) is connected with a steam-water separator (9), a platform (10) is arranged at the top of the shell (2), and the steam-water separator (9) is placed on the platform (10), the biogas digester is characterized in that a biogas digester (11) is arranged at the top of the biogas digester (9), an internal circulation ascending pipe (12) is arranged on one side of the biogas digester (9), the internal circulation ascending pipe (12) penetrates through the three-phase separator device (3), a water collecting tank (13) is arranged at the top in the shell (2), a water outlet pipe (14) is connected to the water collecting tank (13), an external circulation pipe (15) penetrates through the shell (2), valves (20) are arranged on the external circulation pipe (15) and the water outlet pipe (14), the external circulation pipe (15) is located below the three-phase separator device (3), and a sampling pipe (16) is arranged below the external circulation pipe (15).
2. A three-phase separator with good stability for anaerobic towers according to claim 1, characterized by the fact that the angle of the collecting hood (4) is 60 degrees.
3. A three-phase separator with good stability for anaerobic towers according to claim 2, characterized in that the spacing between the gas-collecting channels (4) is 0.2 meters.
4. A three-phase separator for anaerobic columns with good stability according to claim 3, characterized in that the opening of the gas collecting channel (4) is 0.4 meters.
5. A three-phase separator for anaerobic towers with good stability according to claim 4, characterized by that the number of said steam-water separators (9) is two.
6. A three-phase separator with good stability for an anaerobic tower according to claim 5, characterized in that the top of the three-phase separator device (3) is provided with a first three-phase separator pressing beam (18), the bottom of the three-phase separator device (3) is provided with a second three-phase separator pressing beam (17), and the side of the second three-phase separator pressing beam (17) far away from the three-phase separator device (3) is symmetrically provided with a three-phase separator bearing beam (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920054281.7U CN209906436U (en) | 2019-01-08 | 2019-01-08 | Good three-phase separator who is used for anaerobic tower of stability |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920054281.7U CN209906436U (en) | 2019-01-08 | 2019-01-08 | Good three-phase separator who is used for anaerobic tower of stability |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209906436U true CN209906436U (en) | 2020-01-07 |
Family
ID=69029221
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920054281.7U Active CN209906436U (en) | 2019-01-08 | 2019-01-08 | Good three-phase separator who is used for anaerobic tower of stability |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209906436U (en) |
-
2019
- 2019-01-08 CN CN201920054281.7U patent/CN209906436U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN209906436U (en) | Good three-phase separator who is used for anaerobic tower of stability | |
| CN101585601B (en) | Monomer ultra-large volume steel post cone high-temperature anaerobic fermentation system | |
| CN203639240U (en) | Small town domestic sewage treatment system using composite biological constructed wetland | |
| CN203582582U (en) | UASB (upflow anaerobic sludge blanket) anaerobic reactor | |
| CN202766357U (en) | Anaerobic treatment device of acrylic acid and ester mixing production waste water | |
| CN201899941U (en) | Corrugated plate type efficient gas-liquid separator | |
| CN209890342U (en) | Three-phase separator for water treatment | |
| CN114772719A (en) | Multistage fan blade staggered and partitioned efficient anaerobic reactor and treatment method thereof | |
| CN219526388U (en) | Novel high-load anaerobic reactor | |
| CN209065528U (en) | UASB anaerobic biological reactor | |
| CN109806754B (en) | Desulfurizing absorption tower device | |
| CN110963567A (en) | Lifting rotational flow water distribution system of UASB anaerobic reactor | |
| CN221254221U (en) | Integrated equipment suitable for rural small-size sewage treatment | |
| CN201433133Y (en) | Anaerobic baffle reactor | |
| CN211004762U (en) | Self-circulation anaerobic reactor | |
| CN200985331Y (en) | Sewage gas generating device with self-sealing type feeding and gas-collecting device | |
| CN215975167U (en) | IC anaerobic jar gas-water separation equipment | |
| CN209906435U (en) | Anaerobic tower with steady flow function | |
| CN216764624U (en) | Waste water anaerobic treatment pipeline system | |
| CN103803702B (en) | Small mechanized anaerobic reactor | |
| CN221254213U (en) | Anaerobic tank three-phase separator capable of preventing leakage of air and mud | |
| CN209740914U (en) | Household septic tank suitable for rural use | |
| CN204051385U (en) | A kind of waste gas purification apparatus | |
| CN203781910U (en) | Small equipment anaerobic reactor | |
| CN213085583U (en) | Improved upflow anaerobic reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |