CN217351091U - Spiral-flow type internal circulation anaerobic equipment for organic wastewater treatment - Google Patents
Spiral-flow type internal circulation anaerobic equipment for organic wastewater treatment Download PDFInfo
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- CN217351091U CN217351091U CN202220780825.XU CN202220780825U CN217351091U CN 217351091 U CN217351091 U CN 217351091U CN 202220780825 U CN202220780825 U CN 202220780825U CN 217351091 U CN217351091 U CN 217351091U
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- Y—GENERAL 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
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract
The utility model relates to an organic waste water treatment technical field just discloses a spiral-flow type inner loop anaerobism equipment for organic waste water treatment, including anaerobic tower, play mill weir and three-phase separator, it installs in the top of anaerobic tower to go out the mill weir, three-phase separator installs in the inside of anaerobic tower, the internally mounted of anaerobic tower has the waste water treatment subassembly, the waste water treatment subassembly includes water conservancy diversion umbrella, water inlet, back flow, gas collecting channel, air-lift pipe, gas-water separation room, marsh gas water seal room and marsh gas mouth two, water conservancy diversion umbrella fixed connection is in the inner wall bottom of anaerobic tower. This a spiral-flow type inner loop anaerobic equipment for organic waste water treatment handles organic waste water through using the anaerobism, can produce marsh gas at waste water treatment's in-process to with organic waste water resourceization, promoted the benefit of waste water processing, simultaneously through the separation of gas-water separation room, can be so that sewage and marsh gas separation, guaranteed the purity of marsh gas.
Description
Technical Field
The utility model relates to the technical field of organic wastewater treatment, in particular to a spiral-flow type internal circulation anaerobic device for organic wastewater treatment.
Background
The organic wastewater is mainly organic pollutants, and is easy to cause water eutrophication and has large harm. The organic wastewater generally refers to the wastewater discharged by industries such as paper making, leather, food and the like and is more than 2000 mg/L.
In order to ensure the harmless discharge of the wastewater, the wastewater is treated by adopting an anaerobic tower, and the existing anaerobic tower cannot separate methane from the wastewater in the wastewater treatment process, so that the anaerobic tower has certain limitation.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a spiral-flow type inner loop anaerobism equipment for organic waste water treatment to solve the problem that provides among the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a spiral-flow type inner loop anaerobic equipment for organic waste water treatment, includes anaerobic tower, play weir and three phase separator, it installs in the top of anaerobic tower to go out the weir, three phase separator installs in the inside of anaerobic tower, the internally mounted of anaerobic tower has the waste water treatment subassembly.
The waste water treatment assembly comprises a diversion umbrella, a water inlet, a backflow pipe, a gas collecting hood, a gas lift pipe, a gas-water separation chamber, a methane water sealing chamber and a methane port II, wherein the diversion umbrella is fixedly connected to the bottom of the inner wall of the anaerobic tower, the water inlet is arranged in the diversion umbrella, the backflow pipe is arranged in the anaerobic tower, the gas collecting hood is arranged on the outer wall of the backflow pipe, the gas lift pipe is arranged in the backflow pipe, the gas-water separation chamber is fixedly connected to the top of the water outlet weir, the methane water sealing chamber is fixedly connected to the top of the water outlet weir, and the methane port II is arranged at the top of the left side of the methane water sealing chamber.
Preferably, a water outlet is arranged on the left side of the water outlet weir, and the three-phase separator consists of an inclined plate, a first methane port and a lifting plate.
Preferably, the inclined plate is installed inside the three-phase separator, the first methane port is opened inside the three-phase separator, and the lifting plate is installed inside the three-phase separator.
Preferably, the water inlet penetrates through the diversion umbrella and the bottom of the interior of the anaerobic tower and is communicated with an external pressure pump, and waste water and anaerobism can be conveyed to the interior of the anaerobic tower by starting the external pressure pump.
Preferably, the top end of the return pipe penetrates through the top of the inner walls of the three-phase separator and the effluent weir and extends to the upper part of the effluent weir.
Preferably, the number of the gas collecting hoods is two, the two gas collecting hoods are positioned above the three-phase separator, and gas pipes are arranged inside and at the bottom of each gas collecting hood and can be used for collecting methane.
Preferably, the gas stripping pipe is communicated with the gas pipe, the methane collected by the gas pipe can be conveyed to the inside of the gas stripping pipe, the top end of the gas stripping pipe penetrates through the bottom of the gas-water separation chamber and extends to the inside of the gas-water separation chamber, and the methane in the gas stripping pipe can be conveyed to the inside of the gas-water separation chamber and is subjected to gas-water separation in the gas-water separation chamber.
Preferably, the pipeline is installed on the outer wall of the gas-water separation chamber, the pipeline penetrates through the outer wall of the biogas water seal chamber and extends into the biogas water seal chamber, and biogas in the gas-water separation chamber can be conveyed into the biogas water seal chamber through the pipeline.
The utility model provides a spiral-flow type inner loop anaerobic equipment for organic waste water treatment, this a spiral-flow type inner loop anaerobic equipment for organic waste water treatment possesses following beneficial effect:
1. this a spiral-flow type inner loop anaerobic equipment for organic waste water treatment handles organic waste water through using the anaerobism, can produce marsh gas at waste water treatment's in-process to with organic waste water resourceization, promoted the benefit of waste water processing, simultaneously through the separation of gas-water separation room, can be so that sewage and marsh gas separation, guaranteed the purity of marsh gas.
2. This a spiral-flow type inner loop anaerobic equipment for organic waste water handles through using the triphase separator to handle sewage, can maintain better waste water flow state for granular sludge is changeed and is formed and maintain.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the description of the embodiments will be briefly introduced 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 inventive effort.
FIG. 1 is a front view of the overall structure of the present invention;
FIG. 2 is a schematic view of the front side of the internal structure of the anaerobic tower of the present invention;
FIG. 3 is a schematic top view of the structure of the three-phase separator of the present invention;
FIG. 4 is a front partial enlarged schematic view of the wastewater treatment assembly of the present invention.
In the figure: 1. an anaerobic tower; 2. an effluent weir; 3. a three-phase separator; 301. a sloping plate; 302. a methane port I; 303. raising a plate; 4. a wastewater treatment component; 401. a flow guiding umbrella; 402. a water inlet; 403. a return pipe; 404. a gas-collecting hood; 405. a gas stripping pipe; 406. a gas-water separation chamber; 407. a biogas water seal chamber; 408. and a methane port II.
Detailed Description
As shown in fig. 1-4, the utility model provides a technical solution: the utility model provides a spiral-flow type inner loop anaerobic equipment for organic waste water treatment, including anaerobic tower 1, play mill weir 2 and three phase separator 3, it installs in the top of anaerobic tower 1 to go out mill weir 2, the delivery port is installed in the left side of play mill weir 2, three phase separator 3 is installed in anaerobic tower 1's inside, three phase separator 3 is by swash plate 301, marsh gas mouth 302 and kickboard 303, swash plate 301 installs in three phase separator 3's inside, marsh gas mouth 302 is seted up in three phase separator 3's inside, kickboard 303 is installed in three phase separator 3's inside, the internally mounted of anaerobic tower 1 has waste water treatment component 4.
The wastewater treatment component 4 comprises a diversion umbrella 401, a water inlet 402, a return pipe 403, a gas collecting hood 404, a gas stripping pipe 405, a gas-water separation chamber 406, a biogas water seal chamber 407 and a biogas outlet II 408, the diversion umbrella 401 is fixedly connected to the bottom of the inner wall of the anaerobic tower 1, the water inlet 402 is arranged inside the diversion umbrella 401, the water inlet 402 penetrates through the diversion umbrella 401 and the bottom of the anaerobic tower 1 and is communicated with an external pressure pump, wastewater and anaerobe can be conveyed into the anaerobic tower 1 by starting the external pressure pump, the return pipe 403 is arranged inside the anaerobic tower 1, the top end of the return pipe 403 penetrates through the tops of the inner walls of the three-phase separator 3 and the water outlet weir 2 and extends to the upper part of the water outlet weir 2, the gas collecting hoods 404 are arranged on the outer wall of the return pipe 403, the number of the gas collecting hoods 404 is two, the two gas collecting hoods 404 are arranged above the three-phase separator 3, and gas pipes are arranged inside and at the bottom of the gas collecting hoods 404, the biogas can be collected, the gas stripping pipe 405 is arranged inside the return pipe 403, the gas stripping pipe 405 is communicated with a gas pipe, the biogas collected by the gas pipe can be conveyed into the gas stripping pipe 405, the gas-water separation chamber 406 is fixedly connected to the top of the effluent weir 2, the top end of the gas stripping pipe 405 penetrates through the bottom of the gas-water separation chamber 406 and extends into the gas-water separation chamber 406, the biogas inside the gas stripping pipe 405 can be conveyed into the gas-water separation chamber 406 and is subjected to gas-water separation inside the gas-water separation chamber 406, a pipeline is arranged on the outer wall of the gas-water separation chamber 406, the biogas water sealing chamber 407 is fixedly connected to the top of the effluent weir 2, the pipeline penetrates through the outer wall of the biogas water sealing chamber 407 and extends into the biogas water sealing chamber 407, the biogas inside the gas-water separation chamber 406 can be conveyed into the biogas chamber 407 through the pipeline, the biogas port II 408 is arranged at the top of the left side of the biogas water sealing chamber 407, through using the anaerobism to handle organic waste water, can produce marsh gas at waste water treatment's in-process to with organic waste water resourceization, promoted the benefit of waste water processing, simultaneously through the separation of gas-water separation chamber 406, can make sewage and marsh gas separation, guaranteed the purity of marsh gas, handle sewage through using three-phase separator 3, can maintain better waste water flow state, make granular sludge change formation and maintain.
When in use, sewage is conveyed to the inside of the anaerobic tower 1 through the external pressure pump and the water inlet 402, then the anaerobic is conveyed to the inside of the anaerobic tower 1, the anaerobic and the organic sewage react and are treated through the three-phase separator 3, so that the sewage generates methane in the treatment process, the methane is conveyed to the inside of the gas-water separation chamber 406 through the gas stripping pipe 405, then the methane is conveyed to the inside of the methane water sealing chamber 407 through a pipeline and is discharged through the methane outlet II 408, and the organic sewage after treatment flows to the inside of the effluent weir 2 and is discharged through the water outlet inside the effluent weir 2.
Claims (8)
1. The utility model provides a spiral-flow type inner loop anaerobic equipment for organic waste water treatment, includes anaerobic tower (1), play weir (2) and three-phase separator (3), its characterized in that: the effluent weir (2) is arranged at the top of the anaerobic tower (1), the three-phase separator (3) is arranged in the anaerobic tower (1), and the wastewater treatment component (4) is arranged in the anaerobic tower (1);
the wastewater treatment component (4) comprises a diversion umbrella (401), a water inlet (402), a return pipe (403), a gas collecting hood (404), a gas stripping pipe (405), a gas-water separation chamber (406), a biogas water seal chamber (407) and a biogas port II (408), the diversion umbrella (401) is fixedly connected with the bottom of the inner wall of the anaerobic tower (1), the water inlet (402) is arranged inside the diversion umbrella (401), the return pipe (403) is arranged inside the anaerobic tower (1), the gas collecting hood (404) is arranged on the outer wall of the return pipe (403), the gas stripping pipe (405) is arranged inside the return pipe (403), the gas-water separation chamber (406) is fixedly connected with the top of the effluent weir (2), the biogas water seal chamber (407) is fixedly connected with the top of the water outlet weir (2), and the methane port II (408) is arranged at the top of the left side of the methane water sealing chamber (407).
2. The cyclone-type internal circulation anaerobic apparatus for organic wastewater treatment according to claim 1, wherein: a water outlet is arranged on the left side of the water outlet weir (2), and the three-phase separator (3) is composed of an inclined plate (301), a methane port I (302) and a lifting plate (303).
3. The cyclone-type internal circulation anaerobic apparatus for organic wastewater treatment according to claim 2, wherein: the inclined plate (301) is installed inside the three-phase separator (3), the methane port I (302) is arranged inside the three-phase separator (3), and the lifting plate (303) is installed inside the three-phase separator (3).
4. The cyclone-type internal circulation anaerobic apparatus for organic wastewater treatment according to claim 1, wherein: the water inlet (402) penetrates through the diversion umbrella (401) and the bottom of the interior of the anaerobic tower (1) and is communicated with an external pressure pump.
5. The cyclone-type internal circulation anaerobic apparatus for organic wastewater treatment according to claim 1, wherein: the top end of the return pipe (403) penetrates through the top of the inner walls of the three-phase separator (3) and the effluent weir (2) and extends to the upper part of the effluent weir (2).
6. The cyclone-type internal circulation anaerobic apparatus for organic wastewater treatment according to claim 1, wherein: the number of the gas collecting hoods (404) is two, the two gas collecting hoods (404) are positioned above the three-phase separator (3), and gas pipes are arranged inside and at the bottom of each gas collecting hood (404).
7. The cyclone-type internal circulation anaerobic apparatus for organic wastewater treatment according to claim 1, wherein: the gas stripping pipe (405) is communicated with the gas pipe, and the top end of the gas stripping pipe (405) penetrates through the bottom of the gas-water separation chamber (406) and extends to the inside of the gas-water separation chamber (406).
8. The cyclone-type internal circulation anaerobic apparatus for organic wastewater treatment according to claim 1, wherein: and a pipeline is arranged on the outer wall of the gas-water separation chamber (406), penetrates through the outer wall of the biogas water seal chamber (407), and extends to the inside of the biogas water seal chamber (407).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220780825.XU CN217351091U (en) | 2022-04-06 | 2022-04-06 | Spiral-flow type internal circulation anaerobic equipment for organic wastewater treatment |
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| CN202220780825.XU CN217351091U (en) | 2022-04-06 | 2022-04-06 | Spiral-flow type internal circulation anaerobic equipment for organic wastewater treatment |
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| CN217351091U true CN217351091U (en) | 2022-09-02 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118184007A (en) * | 2024-05-20 | 2024-06-14 | 河南环科环保技术有限公司 | Anaerobic reaction device for treating high-concentration organic wastewater and treatment process thereof |
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2022
- 2022-04-06 CN CN202220780825.XU patent/CN217351091U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118184007A (en) * | 2024-05-20 | 2024-06-14 | 河南环科环保技术有限公司 | Anaerobic reaction device for treating high-concentration organic wastewater and treatment process thereof |
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Effective date of registration: 20230105 Address after: 518000 Unit 3510-260, Luohu Business Center, No. 2028, Shennan East Road, Chengdong Community, Dongmen Street, Luohu District, Shenzhen, Guangdong Patentee after: Gulfstream smart environment (Shenzhen) Co.,Ltd. Patentee after: Gulfstream Ecological Environment Management (Guangdong) Co.,Ltd. Address before: 518000 C, floor 3, plant 2, YUDAFU Industrial Park, No. 10, Xingye West Road, Heyi community, Shajing street, Bao'an District, Shenzhen, Guangdong Province Patentee before: Gulfstream smart environment (Shenzhen) Co.,Ltd. |
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