CN214936396U - Anaerobic reactor - Google Patents
Anaerobic reactor Download PDFInfo
- Publication number
- CN214936396U CN214936396U CN202121301686.XU CN202121301686U CN214936396U CN 214936396 U CN214936396 U CN 214936396U CN 202121301686 U CN202121301686 U CN 202121301686U CN 214936396 U CN214936396 U CN 214936396U
- Authority
- CN
- China
- Prior art keywords
- casing
- phase separator
- mixer
- anaerobic reactor
- pipe
- 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
Images
Abstract
The utility model relates to an anaerobic reactor, including casing, three-phase separator, inlet tube, mud pipe and mixer, the mixer is installed on the lateral wall of casing bottom, the output of mixer stretches into in the casing and connects the paddle, the bottom at the casing is installed to the inlet tube, the mud pipe is installed on the lateral wall at casing middle part, the inside top of casing sets up the three-phase separator, the discharge is connected to the three-phase separator, the discharge stretches out the casing top, the casing top sets up a plurality of play mill weirs. The utility model discloses anaerobic reactor adopts side income formula mixer, guarantees the intensive mixing of the inside muddy water of anaerobism cell body, has improved the effective volume in anaerobism cell, need not produce the backward flow of water, need not complicated water distribution system, row's mud system, and the automation requirement is lower, and area is little.
Description
Technical Field
The utility model relates to a sewage treatment technical field, concretely relates to anaerobic reactor.
Background
At the present stage, the concentration of organic matters in industrial production wastewater is higher and higher, so that an anaerobic bioreactor for treating high-concentration organic wastewater has important research and development significance, but the existing anaerobic reactor is complex in structural design, large in occupied area and low in anaerobic treatment efficiency.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an anaerobic reactor for solve the anaerobic reactor structural design among the prior art complicated, problem that area is big.
The utility model provides an anaerobic reactor, including casing, three-phase separator, inlet tube, mud pipe and mixer, the mixer is installed on the lateral wall of casing bottom, the output of mixer stretches into in the casing and connects the paddle, the bottom at the casing is installed to the inlet tube, the mud pipe is installed on the lateral wall at casing middle part, the inside top of casing sets up the three-phase separator, the discharge is connected to the three-phase separator, the discharge stretches out the casing top, the casing top sets up a plurality of play mill weirs.
Furthermore, the three-phase separator is provided with a high layer and a low layer, and the two layers are arranged in a staggered mode.
Furthermore, the top end of the high-rise three-phase separator is connected with a gas collecting pipe, an opening is formed in the upper portion of the low-rise three-phase separator and connected with an exhaust pipe, and a gas outlet of the exhaust pipe is located below the upper-rise three-phase separator.
Further, still include a plurality of sampling tubes, the introduction port of sampling tube is in not co-altitude, the sampling tube is L shape, set up the opening on the casing lateral wall and be used for the sampling tube to stretch out.
Furthermore, the water outlet weir also comprises a water outlet pipe, and the clean water of the water outlet weir is finally discharged through the water outlet pipe.
Adopt above-mentioned the utility model discloses technical scheme's beneficial effect is:
the utility model discloses anaerobic reactor adopts side income formula mixer, guarantees the intensive mixing of the inside muddy water of anaerobism cell body, has improved the effective volume in anaerobism cell, need not produce the backward flow of water, need not complicated water distribution system, row's mud system, and the automation requirement is lower, and area is little.
Drawings
FIG. 1 is a schematic structural view of an anaerobic reactor of the present invention;
in the drawings, the components represented by the respective reference numerals are listed below:
1-shell, 2-three-phase separator, 3-water inlet pipe, 4-sludge discharge pipe, 5-stirrer, 6-paddle, 7-gas collecting pipe, 8-effluent weir, 9-exhaust pipe, 10-sampling pipe and 11-water discharge pipe.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention.
As shown in fig. 1, the utility model provides an anaerobic reactor, including casing 1, three-phase separator 2, inlet tube 3, mud pipe 4 and mixer 5, mixer 5 installs on the lateral wall of casing 1 bottom, the output of mixer 5 stretches into casing 1 and connects paddle 6, inlet tube 3 installs the bottom at casing 1, mud pipe 4 installs on the lateral wall at casing 1 middle part, the inside top of casing 1 sets up three-phase separator 2, gas collecting pipe 7 is connected to three-phase separator 2, gas collecting pipe 7 stretches out casing 1 top, casing 1 top sets up a plurality of water outlet weirs 8.
Specifically, three-phase separator 2 sets up two-layer high-low, and two-layer crisscross setting, discharge 7 is connected on 2 tops of high-rise three-phase separator, the middle upper side of low-rise three-phase separator 2 sets up the opening, and blast pipe 9 is connected to this opening part, the gas outlet of blast pipe 9 is located the below of upper three-phase separator 2.
The working principle of the anaerobic reactor is as follows: waste water flows into the reactor through the water inlet pipe 3, the side-in type stirrer 5 stirs the waste water, no dead zone is left in the reactor, the waste water forms a mud, water and gas three-phase mixture after anaerobic biological metabolism is finished, three-phase separation of mud, water and gas is carried out at the position of the three-phase separator 2, gas at the top end in the low-layer three-phase separator 2 is discharged into the high-layer three-phase separator 2 through the exhaust pipe 9 and is finally discharged together with gas separated by the high-layer three-phase separator 2 through the gas collecting pipe 7, clear water flows into the clear water area upwards through gaps between the three-phase separators 2 and flows into the effluent weir 8, and the sludge slides downwards and is discharged out of the system through the sludge discharge pipe 4.
Preferably, still include a plurality of sampling tubes 10, the sample inlet of sampling tube 10 is in different heights for draw different height samples in real time and detect, sampling tube 10 is the L shape, set up the opening on the 1 lateral wall of casing and be used for sampling tube 10 to stretch out.
Specifically, the device further comprises a drain pipe 11, and the clean water in the effluent weir 8 is finally discharged through the drain pipe 11.
To sum up, the utility model discloses anaerobic reactor adopts side income formula mixer, guarantees the intensive mixing of the inside muddy water of anaerobic cell body, has improved the effective volume of anaerobic tank, does not need the backward flow of product water, especially does not need the area of very big three-phase separator to the transformation of the not high anaerobic system of cell body, need not complicated water distribution system, row's mud system, and the requirement for automation is lower, and area is little; can be used for treating high-concentration nondegradable wastewater with relatively high load.
Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit the same; although the present invention has been described in detail with reference to the foregoing embodiments, it should be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; such modifications and substitutions do not depart from the spirit and scope of the present invention.
Claims (5)
1. The utility model provides an anaerobic reactor, its characterized in that, includes casing, three-phase separator, inlet tube, mud pipe and mixer, the mixer is installed on the lateral wall of casing bottom, the output of mixer stretches into in the casing and connects the paddle, the bottom at the casing is installed to the inlet tube, the mud pipe is installed on the lateral wall at casing middle part, the inside top of casing sets up the three-phase separator, the discharge is connected to the three-phase separator, the discharge stretches out the casing top, the casing top sets up a plurality of play weir.
2. An anaerobic reactor according to claim 1, wherein the three-phase separator is provided with two high and low layers, and the two layers are staggered.
3. An anaerobic reactor according to claim 2, characterized in that the top end of the three-phase separator at the upper layer is connected with a gas collecting pipe, an opening is arranged above the three-phase separator at the lower layer, the opening is connected with a gas outlet pipe, and the gas outlet of the gas outlet pipe is positioned below the three-phase separator at the upper layer.
4. The anaerobic reactor according to claim 1, further comprising a plurality of sampling tubes, wherein the sampling ports of the sampling tubes are at different heights, the sampling tubes are L-shaped, and the side wall of the housing is provided with an opening for the sampling tubes to extend out.
5. An anaerobic reactor according to claim 1, further comprising a drain through which the clear water from the weir is eventually discharged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121301686.XU CN214936396U (en) | 2021-06-10 | 2021-06-10 | Anaerobic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121301686.XU CN214936396U (en) | 2021-06-10 | 2021-06-10 | Anaerobic reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214936396U true CN214936396U (en) | 2021-11-30 |
Family
ID=79053962
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121301686.XU Active CN214936396U (en) | 2021-06-10 | 2021-06-10 | Anaerobic reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214936396U (en) |
-
2021
- 2021-06-10 CN CN202121301686.XU patent/CN214936396U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4966968B2 (en) | Anaerobic purification device | |
| CN101691256B (en) | Tri-phase separator of anaerobic reactor | |
| CN107381807A (en) | A kind of first lattice up-flow combination deflection plate anaerobic hydrolysis reaction integrated apparatus | |
| CN104743745B (en) | A kind of garlic wastewater advanced treatment system | |
| CN219907230U (en) | IC anaerobic reactor for high concentration waste water treatment | |
| CN106966490A (en) | A kind of high-efficiency aerobic reactor and sewage treatment process | |
| CN214936396U (en) | Anaerobic reactor | |
| CN210313698U (en) | Anaerobic reactor | |
| CN2484312Y (en) | Tubelide anaerobic baffling reaction apparatus | |
| CN108905599B (en) | Internal circulation biological desulfurization reactor and method | |
| CN204897529U (en) | STREAMING anaerobic sludge bed reactor in two backward flows | |
| CN114275890A (en) | High-efficiency skid-mounted three-phase separator in high-load anaerobic system | |
| CN204939083U (en) | A kind of eddy flow sludge classification anaerobic ammonia oxidation reactor | |
| CN107973399A (en) | A kind of high-efficiency three-phase piece-rate system | |
| CN201962117U (en) | Multiphase serial internal circulating anaerobic reactor | |
| CN201473355U (en) | Integrated multifunctional air floatation water purifier | |
| CN216997854U (en) | Reaction device for treating garbage leakage liquid | |
| CN201458822U (en) | Integral three-phase separating arrangement of vertical anaerobic treatment tank | |
| CN105692895B (en) | A kind of anaerobism is interior to recycle hydrogen-manufacturing reactor | |
| CN104150648A (en) | Integral pretreatment device for leachate in waste incineration power plant | |
| CN100337938C (en) | Bioreactor for water treatment | |
| CN219526388U (en) | Novel high-load anaerobic reactor | |
| CN105198176B (en) | The regulation and control method of sulfur-bearing nitrogenous effluent is processed using treatment of Organic Wastewater socket type split-phase anaerobic reactor | |
| CN203159323U (en) | Efficient anaerobic reactor | |
| CN213771485U (en) | Anaerobic reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |