CN117209053A - Embedded aeration precipitation integrated self-coagulation activated sludge biochemical reactor - Google Patents
Embedded aeration precipitation integrated self-coagulation activated sludge biochemical reactor Download PDFInfo
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- CN117209053A CN117209053A CN202311473495.5A CN202311473495A CN117209053A CN 117209053 A CN117209053 A CN 117209053A CN 202311473495 A CN202311473495 A CN 202311473495A CN 117209053 A CN117209053 A CN 117209053A
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- biochemical
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- precipitation
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- 239000010802 sludge Substances 0.000 title claims abstract description 198
- 238000001556 precipitation Methods 0.000 title claims abstract description 38
- 238000005273 aeration Methods 0.000 title claims abstract description 20
- 238000005345 coagulation Methods 0.000 title claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 71
- 238000004062 sedimentation Methods 0.000 claims abstract description 39
- 238000012216 screening Methods 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 238000000926 separation method Methods 0.000 claims abstract description 12
- 238000005276 aerator Methods 0.000 claims abstract description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000001301 oxygen Substances 0.000 claims abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 4
- 238000010992 reflux Methods 0.000 claims description 9
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000005842 biochemical reaction Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 244000005700 microbiome Species 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 238000004220 aggregation Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The application discloses an embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor which comprises a biochemical tank, a precipitation module and an aerator, wherein the water inlet end of the biochemical tank is connected with an upper-level processing unit, and the water outlet end of the biochemical tank is connected with a lower-level processing unit; the sedimentation module is fixedly arranged in the biochemical tank, and a water inlet area, a mud-water separation area, a flocculated sludge area, a compact sludge area and a water collecting area are arranged in the sedimentation module; the sedimentation module is used for carrying out mud-water separation on the mixed liquid in the biochemical tank and screening compact sludge and floccule sludge on the separated sludge; the aerator is fixedly arranged at the bottom of the biochemical tank and is used for supplying oxygen to the activated sludge in the biochemical tank. The application is provided with the sedimentation module in the biochemical tank, thereby realizing the functions of aerobic biochemical reaction of activated sludge and sedimentation and separation of sludge into a whole and saving the occupied area; the sludge cyclone separator is utilized to screen the flocculated sludge secondarily, and the screening efficiency is improved through the two-stage screening of the precipitation module and the sludge cyclone separator.
Description
Technical Field
The application relates to the technical field of sewage treatment equipment, in particular to an embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor.
Background
The aerobic compact sludge is a special microorganism aggregate which has granular regular appearance, compact structure, excellent sedimentation performance and obvious pollutant treatment effect and is formed by self-aggregation under the aerobic condition, namely the microorganism self-fixation forms a special process of organism aggregation under the hydrodynamic condition, and compared with the traditional activated sludge process, the aerobic compact sludge is difficult to have the problems of sludge expansion, poor treatment water quality and the like. The overall energy consumption of the aerobic compact sludge system is low, and the effluent quality can reach even better than that of the traditional activated sludge process. The sludge is cultivated under the aerobic condition, and the layered structure of the compact sludge forms aerobic, anoxic and anaerobic areas, and the structural characteristics of the compact sludge can realize the denitrification and dephosphorization effects to a certain extent. The volume required by the aerobic compact sludge system is lower than that required by the conventional activated sludge device, and the energy consumption and the civil engineering cost are reduced. By controlling the operation of the reactor, the flocculent sludge with small density and poor sedimentation performance is discharged out of the biochemical system, and the compact sludge with high quality and large particle size is kept in the biochemical system.
However, the factors influencing the formation of the aerobic compact sludge are complex and variable, the control of the operation conditions is severe, and the like, if the operation parameters are controlled improperly, the sludge is disintegrated, and the quality of the effluent water is deteriorated. Therefore, in order to keep the aerobic compact sludge with good performance and compact structure in a biochemical system, the activated low-activity loose floccule sludge needs to be discharged out of the system, and thus the sludge needs to be screened. The existing screening mode is to connect a secondary sedimentation tank behind a conventional biochemical tank, but the secondary sedimentation tank almost completely sediments the mixed liquid sludge, so that dense sludge and flocculated sludge cannot be screened, and the dense activated sludge is difficult to culture and screen. It is therefore desirable to provide an activated sludge biochemical reactor to solve the above-mentioned technical problems.
Disclosure of Invention
The application aims to provide an embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor so as to solve the problems in the prior art.
In order to achieve the above purpose, the application provides an embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor, which comprises:
the water inlet end of the biochemical tank is connected with the upper-level processing unit, and the water outlet end of the biochemical tank is connected with the lower-level processing unit;
the sedimentation module is fixedly arranged in the biochemical tank, and a water inlet area, a mud-water separation area, a floccule sludge area, a compact sludge area and a water collecting area are arranged in the sedimentation module; the sedimentation module is used for carrying out mud-water separation on the mixed liquid in the biochemical tank and screening compact sludge and floccule sludge on the separated sludge;
the aerator is fixedly arranged at the bottom of the biochemical tank and is used for supplying oxygen to the activated sludge in the biochemical tank.
Preferably, the sedimentation module comprises a shell, openings are formed in the upper end and the lower end of the shell, the top end of the shell is higher than the water level of the biochemical pond, and a plurality of V-shaped sedimentation hoppers are fixedly connected to the opening at the bottom end of the shell; a plurality of mixed liquid water inlets are formed in two opposite side walls of the bottom of the shell, a water drainage groove is formed in the top of the inner side of the shell, a water outlet pipe is fixedly communicated with the bottom end of the water drainage groove, a water collecting channel is fixedly arranged on the inner wall of the upper part of the biochemical pond, and the water drainage groove is communicated with the water collecting channel through the water outlet pipe; the bottom side wall of the shell is fixedly communicated with a floc sludge mixed liquid lifting pipe, the bottom of the V-shaped sludge settling hopper is fixedly communicated with a compact sludge return pipeline, and the compact sludge return pipeline is communicated with the upper-level processing unit.
Preferably, the shell is internally arranged in a perforated pipe, the middle part of the perforated pipe is fixedly communicated with the floc sludge mixed liquor lifting pipe, and the tail end of the floc sludge mixed liquor lifting pipe is fixedly communicated with a sludge pump.
Preferably, an air feeding pipe is fixedly communicated with the compact sludge return pipeline.
Preferably, a baffle is fixedly connected to the outer wall of the shell, and the baffle is arranged corresponding to the plurality of mixed liquid water inlets.
Preferably, a weir plate is detachably arranged on the drainage groove, and the height of the weir plate is adjustable.
Preferably, the weir plate is a serrated triangular weir or a rectangular weir.
Preferably, the device further comprises a sludge cyclone separator, wherein the sludge cyclone separator is fixedly arranged at the top of the biochemical tank, the bottom end of the sludge cyclone separator is fixedly communicated with a sludge discharge bell mouth, the sludge cyclone separator is communicated with the biochemical tank through the sludge discharge bell mouth, and the top of the sludge cyclone separator is communicated with an overflow port; the outlet end of the sludge pump is provided with a switch discharge electric valve, a reflux electric valve and a floc sludge screening electric valve respectively through four-way joints, the outlet end of the reflux electric valve is communicated with the upper-level processing unit, and the outlet end of the floc sludge screening electric valve is communicated with the sludge cyclone separator.
Preferably, the biochemical tank is internally and fixedly provided with a supporting leg, and the sedimentation module is fixedly connected with the biochemical tank through the supporting leg.
Preferably, the precipitation module is made of stainless steel or plastic.
Compared with the prior art, the application has the following advantages and technical effects:
1. the embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor provided by the application is characterized in that an aerobic tank and a secondary sedimentation tank are combined, a precipitation module is arranged in the biochemical tank, the functions of activated sludge aerobic biochemical reaction and sludge precipitation separation are integrated, and the occupied area is saved.
2. The sedimentation module is utilized to screen out the aerobic compact sludge, the aerobic compact sludge is intercepted and flows back to the upper treatment unit, and the special microorganism aggregate with compact structure, excellent sedimentation performance and obvious pollutant treatment effect is reserved in the system.
3. The sludge cyclone separator is utilized to screen the flocculated sludge secondarily, the secondary compact aerobic sludge is screened out again and returned to the biochemical tank, and the screening efficiency is improved through the two-stage screening of the sedimentation module and the sludge cyclone separator.
Drawings
In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings that are needed 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 application, and other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic diagram of the structure of an embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor;
FIG. 2 is a plan view of the upper layer of the sedimentation module of the present application;
FIG. 3 is a plan view of a layer in a precipitation module according to the present application;
FIG. 4 is a plan view of the lower layer of the sedimentation module of the present application;
FIG. 5 is a cross-sectional view of the sedimentation module of the present application taken along the direction 1-1;
FIG. 6 is a cross-sectional view of the sedimentation module of the present application taken along the direction 2-2;
FIG. 7 is a cross-sectional view of the sedimentation module of the present application taken along the 3-3 direction;
FIG. 8 is a schematic view of the structure of the water outlet weir of the present application;
wherein: 1. a biochemical pool; 2. a sludge cyclone separator; 3. a precipitation module; 4. an aerator; 5. a support leg; 6. v-shaped mud settling hopper; 7. a mixed liquid water inlet hole; 8. a baffle; 9. a drainage channel; 10. a water outlet pipe; 11. a water collecting channel; 12. compact sludge return pipe; 13. an air feeding pipe; 14. a floc sludge mixed liquor lifting pipe; 15. a sludge pump; 16. a discharge electric valve; 17. a back flow electric valve; 18. an electric valve for screening the flocculated sludge; 19. a mud discharging horn mouth; 20. and an overflow port.
Detailed Description
It should be noted that, without conflict, the embodiments of the present application and features of the embodiments may be combined with each other. The described embodiments are only some, but not all, embodiments of the application. All other embodiments, which can be made by those skilled in the art without the inventive effort, are intended to be within the scope of the present application. The application will be described in detail below with reference to the drawings in connection with embodiments.
The application provides an embedded aeration precipitation integrated self-coagulation activated sludge biochemical reactor, which comprises:
the water inlet end of the biochemical tank 1 is connected with the upper-level processing unit, and the water outlet end of the biochemical tank 1 is connected with the lower-level processing unit;
the sedimentation module 3 is fixedly arranged in the biochemical tank 1, and a water inlet area, a mud-water separation area, a floccule sludge area, a compact sludge area and a water collecting area are arranged in the sedimentation module 3; the sedimentation module 3 is used for carrying out mud-water separation on the mixed liquid in the biochemical tank 1 and screening compact sludge and floccule sludge on the separated sludge;
the aerator 4 is fixedly arranged at the bottom of the biochemical tank 1, and the aerator 4 is used for supplying oxygen to the activated sludge in the biochemical tank 1.
Further, the sedimentation module 3 comprises a shell, openings are formed in the upper end and the lower end of the shell, and the top end of the shell is higher than the water level of the biochemical tank 1, so that sewage in the biochemical tank 1 is prevented from being turned up into the sedimentation module 3, and the sedimentation effect of the sedimentation module 3 is prevented from being influenced; a plurality of V-shaped sludge settling hoppers 6 are fixedly connected to the bottom end opening of the shell; a plurality of mixed liquid water inlets 7 are formed in two opposite side walls of the bottom of the shell, a water drainage groove 9 is formed in the top of the inner side of the shell, a water outlet pipe 10 is fixedly communicated with the bottom end of the water drainage groove 9, a water collecting channel 11 is fixedly arranged on the inner wall of the upper part of the biochemical tank 1, and the water drainage groove 9 is communicated with the water collecting channel 11 through the water outlet pipe 10; the bottom side wall of the shell is fixedly communicated with a floc sludge mixed liquid lifting pipe 14, the bottom of the V-shaped sludge settling hopper 6 is fixedly communicated with a compact sludge return pipeline 12, and the compact sludge return pipeline 12 is communicated with an upper-level processing unit.
The mixed liquor enters a sedimentation module 3 through a mixed liquor water inlet hole 7, the lower area of the V-shaped sludge hopper is a compact sludge area, the upper area of the V-shaped sludge hopper is a floc sludge area, the density of sludge is slightly higher than that of water, the compact sludge enters the compact sludge area after sedimentation, and the compact sludge in the V-shaped sludge hopper 6 returns to a superior treatment unit such as an anaerobic tank or an anoxic tank through a compact sludge return pipeline 12 to maintain the concentration of sludge in the whole biochemical system, so that high-quality compact sludge is kept in the whole biochemical system; the flocculated sludge is precipitated and enters a flocculated sludge area, and clarified water flows out through a drainage tank 9.
Further, the inside of the shell is arranged in a perforated pipe, the middle part of the perforated pipe is fixedly communicated with a floc sludge mixed liquor lifting pipe 14, and the tail end of the floc sludge mixed liquor lifting pipe 14 is fixedly communicated with a sludge pump 15. The floc sludge can be extracted relatively uniformly from the floc sludge region by means of perforated pipes.
Further, an air adding pipe 13 is fixedly communicated with the compact sludge reflux pipeline 12, and after air is added through the air adding pipe 13, the density of the air-water mixed solution is lower than that of water, namely, the air stripping method is utilized, so that the compact sludge mixed solution flows upwards to return to the upper-level treatment unit.
Further, a baffle plate 8 is fixedly connected to the outer wall of the shell, and the baffle plate 8 and a plurality of mixed liquid water inlet holes 7 are correspondingly arranged. The baffle 8 can block bubbles in the mixed liquor from entering the sedimentation module 3. And small bubbles in the mixed liquid further separate and float upwards in a water inlet area formed by the baffle plate 8 and the mixed liquid water inlet holes 7, so that the bubbles are prevented from entering the precipitation module 3 to influence sludge precipitation.
Further, a weir plate is detachably arranged on the drainage tank 9, the height of the weir plate is adjustable, and the weir plate is a saw-tooth triangular weir or a rectangular weir. The small flocculent sludge continuously flows upwards along with the mixed liquid and flows to a sludge-water separation area, clarified effluent flows upwards under the action of the weir plate, the clarified effluent is turned into a drainage tank 9 from the upper edge of the weir plate, the small sludge floccules are precipitated at the drainage tank, the small sludge floccules are collided and aggregated to become slightly large sludge floccules, and the slightly large sludge floccules are settled to a floccule sludge area at the upper part of the V-shaped sludge hopper, so that sludge-water separation is realized.
Further, the biochemical treatment device also comprises a sludge cyclone separator 2, wherein the sludge cyclone separator 2 is fixedly arranged at the top of the biochemical pond 1, the bottom end of the sludge cyclone separator 2 is fixedly communicated with a sludge discharge bell mouth 19, the sludge cyclone separator 2 is communicated with the biochemical pond 1 through the sludge discharge bell mouth 19, and the top of the sludge cyclone separator 2 is communicated with an overflow mouth 20; the outlet end of the sludge pump 15 is respectively provided with a switch discharge electric valve 16, a reflux electric valve 17 and a flocculated sludge screening electric valve 18 through a four-way, the outlet end of the reflux electric valve 17 is communicated with the upper-level processing unit, and the outlet end of the flocculated sludge screening electric valve 18 is communicated with the sludge cyclone separator 2.
After the floc sludge is lifted by the sludge pump 15, in the operation process, the first condition is that the discharge electric valve 16 is opened, and the floc sludge is selected to be directly discharged as surplus sludge; in the second case, the reflux electric valve 17 is opened to reflux the flocculated sludge to the upper-level treatment unit; in the third case, an electric valve 18 for screening the flocculated sludge is opened, the flocculated sludge enters a secondary screening unit, namely a sludge cyclone separator 2, a flocculated sludge mixed solution enters the sludge cyclone separator 2 along a tangent line of the wall of the cylinder, external cyclone is generated, some dense sludge with relatively high density is thrown to the periphery, and finally the dense sludge is discharged through a sludge discharge horn mouth 19 at the bottom of the sludge cyclone separator 2 and returns to the biochemical tank 1 through a pipeline, so that the dense sludge with relatively high quality is trapped; the loose sludge flocs are upwards cyclone along with water flow at the center of the sludge cyclone separator 2, and finally the floc sludge is discharged along with an overflow port 20 at the upper part of the sludge cyclone separator 2 and is discharged as surplus sludge.
The electric valve 16, the reflux electric valve 17 or the floc sludge screening electric valve 18 are opened and closed, so that the floc sludge screened out by the first stage of the precipitation module 3 can be reasonably determined to be directly discharged, refluxed or subjected to second-stage floc sludge screening according to the state of the floc sludge, the operation parameters and states of a biochemical system, such as the sludge concentration, the culture condition of compact sludge and the like, so that the operation modes are more diversified.
Further, the support legs 5 are fixedly arranged in the biochemical tank 1, and the sedimentation module 3 is fixedly connected with the biochemical tank 1 through the support legs 5.
Further, the precipitation module 3 is made of stainless steel or plastic.
The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor provided by the application can be used for biochemical units and precipitation separation units for sewage treatment of various scales, high-quality and high-efficiency compact sludge is screened, the treatment efficiency is improved, a plurality of precipitation modules 3 can be arranged in parallel in a large sewage treatment plant, the effluent of each precipitation module 3 is collected into a water collecting channel 11, and the compact sludge separated by each precipitation module 3 is collected into a sludge channel through gas stripping and flows back to a pre-treatment unit.
The present application is not limited to the above-mentioned embodiments, and any changes or substitutions that can be easily understood by those skilled in the art within the technical scope of the present application are intended to be included in the scope of the present application. Therefore, the protection scope of the present application should be subject to the protection scope of the claims.
Claims (10)
1. An embedded aeration precipitation integrated self-coagulation activated sludge biochemical reactor, which is characterized by comprising:
the biochemical treatment device comprises a biochemical pond (1), wherein the water inlet end of the biochemical pond (1) is connected with an upper-level treatment unit, and the water outlet end of the biochemical pond (1) is connected with a lower-level treatment unit;
the sedimentation module (3), the sedimentation module (3) is fixedly arranged in the biochemical tank (1), and a water inlet area, a mud-water separation area, a floccule sludge area, a compact sludge area and a water collecting area are arranged in the sedimentation module (3); the sedimentation module (3) is used for separating mud from water of the mixed liquid in the biochemical tank (1) and screening compact sludge and floccule sludge of the separated sludge;
the aerator (4), the aerator (4) is fixedly arranged at the bottom of the biochemical tank (1), and the aerator (4) is used for supplying oxygen to the activated sludge in the biochemical tank (1).
2. The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor according to claim 1, wherein the precipitation module (3) comprises a shell, openings are formed in the upper end and the lower end of the shell, the top end of the shell is higher than the water level of the biochemical pond (1), and a plurality of V-shaped sludge settling hoppers (6) are fixedly connected to the opening at the bottom end of the shell; a plurality of mixed liquid water inlet holes (7) are formed in two opposite side walls of the bottom of the shell, a water drainage groove (9) is formed in the top of the inner side of the shell, a water outlet pipe (10) is fixedly communicated with the bottom end of the water drainage groove (9), a water collecting channel (11) is fixedly arranged on the inner wall of the upper part of the biochemical tank (1), and the water drainage groove (9) is communicated with the water collecting channel (11) through the water outlet pipe (10); the bottom side wall of the shell is fixedly communicated with a floc sludge mixed liquid lifting pipe (14), the bottom of the V-shaped sludge settling hopper (6) is fixedly communicated with a compact sludge backflow pipeline (12), and the compact sludge backflow pipeline (12) is communicated with the upper-level processing unit.
3. The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor according to claim 2, wherein the inside of the shell is arranged in a perforated pipe, the middle part of the perforated pipe is fixedly communicated with the floc sludge mixed liquor lifting pipe (14), and the tail end of the floc sludge mixed liquor lifting pipe (14) is fixedly communicated with a sludge pump (15).
4. The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor according to claim 2, wherein an air feeding pipe (13) is fixedly communicated with the compact sludge reflux pipeline (12).
5. The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor according to claim 2, wherein a baffle (8) is fixedly connected to the outer wall of the shell, and the baffle (8) is arranged corresponding to a plurality of mixed liquor water inlet holes (7).
6. The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor according to claim 2, wherein a weir plate is detachably arranged on the drainage tank (9), and the height of the weir plate is adjustable.
7. The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor according to claim 6, wherein the weir plate is a serrated triangular weir or a rectangular weir.
8. The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor according to claim 3, further comprising a sludge cyclone (2), wherein the sludge cyclone (2) is fixedly arranged at the top of the biochemical tank (1), a sludge discharge bell mouth (19) is fixedly communicated with the bottom end of the sludge cyclone (2), the sludge cyclone (2) is communicated with the biochemical tank (1) through the sludge discharge bell mouth (19), and an overflow port (20) is communicated with the top of the sludge cyclone (2); the outlet end of the sludge pump (15) is provided with a switch discharge electric valve (16), a return electric valve (17) and a floc sludge screening electric valve (18) respectively through a four-way, the outlet end of the return electric valve (17) is communicated with the upper-level processing unit, and the outlet end of the floc sludge screening electric valve (18) is communicated with the sludge cyclone separator (2).
9. The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor according to claim 1, wherein a supporting leg (5) is fixedly arranged in the biochemical tank (1), and the precipitation module (3) is fixedly connected with the biochemical tank (1) through the supporting leg (5).
10. The embedded aeration and precipitation integrated self-coagulation activated sludge biochemical reactor according to claim 1, wherein the precipitation module (3) is made of stainless steel or plastic.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311473495.5A CN117209053B (en) | 2023-11-08 | 2023-11-08 | Embedded aeration precipitation integrated self-coagulation activated sludge biochemical reactor |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311473495.5A CN117209053B (en) | 2023-11-08 | 2023-11-08 | Embedded aeration precipitation integrated self-coagulation activated sludge biochemical reactor |
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| Publication Number | Publication Date |
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| CN117209053A true CN117209053A (en) | 2023-12-12 |
| CN117209053B CN117209053B (en) | 2024-01-30 |
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| Application Number | Title | Priority Date | Filing Date |
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|---|---|---|---|---|
| GB1355869A (en) * | 1970-06-10 | 1974-06-05 | Stenberg Flygt Ab | Device for purification of sewage |
| JPS583692A (en) * | 1981-06-29 | 1983-01-10 | Ebara Infilco Co Ltd | Method for treating waste water |
| US4818392A (en) * | 1987-11-30 | 1989-04-04 | Hazleton Environmental Products Inc. | Liquid waste treatment system |
| JPH1147787A (en) * | 1997-07-31 | 1999-02-23 | Gouda:Kk | Cleaning system of drainage by function of microorganism |
| CN107973398A (en) * | 2017-11-24 | 2018-05-01 | 中粮生化能源（衡水）有限公司 | A kind of pusher reaction unit and its cultural method for cultivating aerobic particle mud |
| WO2020124635A1 (en) * | 2018-12-18 | 2020-06-25 | 华南理工大学 | Load-enhanced fluidized reaction equipment, system and method for wastewater treatment |
| CN113149194A (en) * | 2021-05-07 | 2021-07-23 | 艾柯环保技术(杭州)有限公司 | Method for promoting two-stage sedimentation of continuous flow aerobic granular sludge |
| CN113304685A (en) * | 2021-06-02 | 2021-08-27 | 浙江大学 | Continuous flow aerobic granular sludge reaction device with stirring paddle internal member and method |
| CN115108675A (en) * | 2022-07-12 | 2022-09-27 | 北京工业大学 | Algae-containing water source water treatment method and system based on high-gradient magnetic separation |
| CN116789263A (en) * | 2023-07-07 | 2023-09-22 | 泛华建设集团有限公司河南分公司 | Activated sludge screening treatment method using densification agent |
-
2023
- 2023-11-08 CN CN202311473495.5A patent/CN117209053B/en active Active
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1355869A (en) * | 1970-06-10 | 1974-06-05 | Stenberg Flygt Ab | Device for purification of sewage |
| JPS583692A (en) * | 1981-06-29 | 1983-01-10 | Ebara Infilco Co Ltd | Method for treating waste water |
| US4818392A (en) * | 1987-11-30 | 1989-04-04 | Hazleton Environmental Products Inc. | Liquid waste treatment system |
| JPH1147787A (en) * | 1997-07-31 | 1999-02-23 | Gouda:Kk | Cleaning system of drainage by function of microorganism |
| CN107973398A (en) * | 2017-11-24 | 2018-05-01 | 中粮生化能源（衡水）有限公司 | A kind of pusher reaction unit and its cultural method for cultivating aerobic particle mud |
| WO2020124635A1 (en) * | 2018-12-18 | 2020-06-25 | 华南理工大学 | Load-enhanced fluidized reaction equipment, system and method for wastewater treatment |
| CN113149194A (en) * | 2021-05-07 | 2021-07-23 | 艾柯环保技术(杭州)有限公司 | Method for promoting two-stage sedimentation of continuous flow aerobic granular sludge |
| CN113304685A (en) * | 2021-06-02 | 2021-08-27 | 浙江大学 | Continuous flow aerobic granular sludge reaction device with stirring paddle internal member and method |
| CN115108675A (en) * | 2022-07-12 | 2022-09-27 | 北京工业大学 | Algae-containing water source water treatment method and system based on high-gradient magnetic separation |
| CN116789263A (en) * | 2023-07-07 | 2023-09-22 | 泛华建设集团有限公司河南分公司 | Activated sludge screening treatment method using densification agent |
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|---|---|
| CN117209053B (en) | 2024-01-30 |
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