CN220564445U - High-efficient integration sewage treatment device - Google Patents
High-efficient integration sewage treatment device Download PDFInfo
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- CN220564445U CN220564445U CN202321618752.5U CN202321618752U CN220564445U CN 220564445 U CN220564445 U CN 220564445U CN 202321618752 U CN202321618752 U CN 202321618752U CN 220564445 U CN220564445 U CN 220564445U
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- pipe
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- 239000010865 sewage Substances 0.000 title claims abstract description 47
- 238000011282 treatment Methods 0.000 title claims abstract description 43
- 230000010354 integration Effects 0.000 title claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 65
- 238000000926 separation method Methods 0.000 claims abstract description 39
- 230000007062 hydrolysis Effects 0.000 claims abstract description 31
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 31
- 238000004062 sedimentation Methods 0.000 claims abstract description 20
- 238000006243 chemical reaction Methods 0.000 claims abstract description 17
- 238000005189 flocculation Methods 0.000 claims abstract description 17
- 230000016615 flocculation Effects 0.000 claims abstract description 17
- 238000005273 aeration Methods 0.000 claims description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 16
- 239000001301 oxygen Substances 0.000 claims description 16
- 229910052760 oxygen Inorganic materials 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 11
- 239000000945 filler Substances 0.000 claims description 8
- 238000004065 wastewater treatment Methods 0.000 claims 6
- 239000004744 fabric Substances 0.000 claims 1
- 238000000354 decomposition reaction Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 description 6
- 230000005484 gravity Effects 0.000 description 5
- 238000005276 aerator Methods 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000020477 pH reduction Effects 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 238000001914 filtration Methods 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000002957 persistent organic pollutant Substances 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000011221 initial treatment Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model discloses high-efficiency integrated sewage treatment equipment, which relates to the technical field of sewage treatment equipment and comprises a hydrolysis treatment tank, wherein the right side of the hydrolysis treatment tank is connected with a decomposition tank, the right side of the decomposition tank is connected with an aerobic zone, the right side of the aerobic zone is connected with a separation zone, the right side of the separation zone is connected with a reaction zone, the right side of the reaction zone is connected with a flocculation zone, the right side of the separation zone is connected with a sedimentation tank, the left side of the hydrolysis treatment tank is connected with an integrated device water inlet, and the right side of the sedimentation tank is connected with an integrated device water outlet.
Description
Technical Field
The utility model relates to the technical field of sewage treatment equipment, in particular to efficient integrated sewage treatment equipment.
Background
According to the classification of sewage sources, sewage treatment is generally divided into production sewage treatment and domestic sewage treatment, wherein the production sewage comprises industrial sewage and agricultural sewage, and the application of sewage treatment equipment can effectively treat the domestic sewage, so that people can live in a clean environment.
However, in the actual use process of the existing integrated sewage treatment equipment, because the integrated sewage treatment equipment generally removes solid pollutants in a suspended state in sewage through a physical treatment method, most of the integrated sewage treatment equipment can only meet the requirement of primary treatment, and the treatment effect is poor.
Therefore, there is an urgent need to design a high-efficiency integrated sewage treatment device to solve the above technical problems.
Disclosure of Invention
The utility model aims to provide efficient integrated sewage treatment equipment so as to solve the problem that the integrated sewage treatment equipment provided in the background art is poor in treatment effect.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a high-efficient integration sewage treatment device, includes the hydrolysis tank, the right side of hydrolysis tank is connected with the decomposer, the right side of decomposer is connected with good oxygen district, good oxygen right side in district is connected with the separation district, the right side in separation district is connected with the reaction district, the right side in reaction district is connected with the flocculation zone, the right side in separation district is connected with the sedimentation tank, the left side of hydrolysis tank is connected with the integrated device water inlet, the right side in sedimentation tank is connected with the integrated device delivery port, the upper end in flocculation zone is provided with first mount, the upper end in sedimentation tank is provided with the second mount.
Further, the bottom of the hydrolysis treatment tank is provided with a first water distribution pipe, the inner side of the hydrolysis treatment tank is connected with a combined filler, the right side of the hydrolysis treatment tank is provided with a first water passing hole, and large particles and suspended matters in sewage can be intercepted by the combined filler, so that the hydrolysis acidification efficiency is improved.
Further, the second water distribution pipe is arranged at the bottom end of the decomposing tank, the second water passing holes are formed in the right side of the decomposing tank, water above the hydrolysis treatment tank can flow into the decomposing tank through the first water passing holes, and accordingly the denitrification process of sewage in the decomposing tank is convenient to complete.
Further, the bottom of good oxygen district is connected with first aeration pipe, the bottom of separation district is connected with the second aeration pipe, the upper end of first aeration pipe and second aeration pipe all is provided with the micropore aeration head, can be to the continuous oxygen of letting in good oxygen district and separation district through the micropore aeration head, is convenient for good oxygen microorganism ingests, decomposes the organic pollutant of absorption.
Further, the right side of good oxygen district is provided with the third and crosses the water hole, the inboard of separation district is provided with up-flow solid-liquid separation module, up-flow solid-liquid separation module's upper end is connected with the blast pipe, the right side of separation district is provided with the fourth and crosses the water hole, the right side of reaction district is provided with the fifth and crosses the water hole, is convenient for carry out the secondary filtration with the pollutant through up-flow solid-liquid separation module for the gaseous follow blast pipe of separation discharges, and sewage gets into the reaction district.
Further, the upper end of first mount is equipped with the mixer, the lower extreme of mixer is connected with the output shaft, the surface of output shaft is provided with the blade, through starting the mixer, can drive the epaxial blade of output and rotate in the flocculation zone.
Further, the back of flocculation zone is connected with the water pipe, the back of water pipe is connected with central water distribution pipe, the bottom of sedimentation tank is connected with the mud pipe, utilizes gravity effect to make the suspension mud that contact oxidation bed goes out water with the specific gravity and is greater than water sink to the bottom of the pool through the sedimentation tank.
Compared with the prior art, the utility model has the beneficial effects that: this high-efficient integration sewage treatment device through setting up hydrolysis tank, decomposer, good oxygen district, separation zone, reaction zone, flocculation zone and sedimentation tank to utilize the combination filler to hold back big particulate matter and suspended solid in the sewage, improve hydrolysis acidification efficiency, still through setting up-flow solid-liquid separation module, be convenient for filter sewage once more, realize the purification of sewage through multilayer treatment, improved the purifying effect of sewage greatly.
Drawings
FIG. 1 is a top view of the present utility model;
FIG. 2 is a plan view of an aerator pipe according to the present utility model;
FIG. 3 is a cross-sectional view of the utility model A-A;
FIG. 4 is a cross-sectional view of the utility model B-B;
FIG. 5 is a cross-sectional view of the utility model C-C.
In the figure: 1. a hydrolysis treatment tank; 2. a decomposing tank; 3. an aerobic zone; 4. a separation zone; 5. a reaction zone; 6. a flocculation zone; 7. a sedimentation tank; 8. a water inlet of the integrated device; 9. a water outlet of the integrated device; 10. a first water distribution pipe; 11. a combined filler; 12. a first water passing hole; 13. a second water distribution pipe; 14. a second water passing hole; 15. a first aerator pipe; 16. a second aerator pipe; 17. a microporous aeration head; 18. a third water passing hole; 19. an upflow solid-liquid separation module; 20. an exhaust pipe; 21. a fourth water passing hole; 22. a fifth water passing hole; 23. a first fixing frame; 24. a stirrer; 25. an output shaft; 26. a blade; 27. a water passing pipe; 28. a central water distribution pipe; 29. the second fixing frame; 30. a mud pipe.
Detailed Description
Referring to fig. 1-5, the present utility model provides a technical solution: the utility model provides a high-efficient integration sewage treatment device, includes hydrolysis tank 1, hydrolysis tank 1's right side is connected with decomposer 2, decomposer 2's right side is connected with good oxygen district 3, good oxygen district 3's right side is connected with separation district 4, separation district 4's right side is connected with reaction district 5, reaction district 5's right side is connected with flocculation zone 6, separation district 4's right side is connected with sedimentation tank 7, hydrolysis tank 1's left side is connected with integrated device water inlet 8, sedimentation tank 7's right side is connected with integrated device delivery port 9, flocculation zone 6's upper end is provided with first mount 23, sedimentation tank 7's upper end is provided with second mount 29.
Meanwhile, the first water distribution pipe 10 is arranged at the bottom end of the hydrolysis treatment tank 1, the combined filler 11 is connected to the inner side of the hydrolysis treatment tank 1, the first water passing holes 12 are formed in the right side of the hydrolysis treatment tank 1, large particles and suspended matters in sewage can be trapped through the combined filler 11, the hydrolysis acidification efficiency is improved, the second water distribution pipe 13 is arranged at the bottom end of the decomposition tank 2, the second water passing holes 14 are formed in the right side of the decomposition tank 2, water above the hydrolysis treatment tank 1 can flow into the decomposition tank 2 through the first water passing holes 12, so that the sewage can be subjected to denitrification in the decomposition tank 2, the first aeration pipe 15 is connected to the bottom end of the aerobic zone 3, the second aeration pipe 16 is connected to the bottom end of the separation zone 4, and microporous aeration heads 17 are arranged at the upper ends of the first aeration pipe 15 and the second aeration pipe 16, and oxygen can be fed into the aerobic zone 3 and the separation zone 4 without interruption through the microporous aeration heads 17, so that the aerobic microorganisms can absorb and decompose the adsorbed organic pollutants.
In addition, the right side of aerobic zone 3 is provided with third water hole 18, the inboard of separation zone 4 is provided with up-flow solid-liquid separation module 19, the upper end of up-flow solid-liquid separation module 19 is connected with blast pipe 20, the right side of separation zone 4 is provided with fourth water hole 21, the right side of reaction zone 5 is provided with fifth water hole 22, be convenient for carry out the secondary filtration to the pollutant through up-flow solid-liquid separation module 19 to make the gaseous exhaust pipe 20 of separation discharge, sewage get into reaction zone 5, the upper end of first mount 23 is equipped with agitator 24, the lower extreme of agitator 24 is connected with output shaft 25, the surface of output shaft 25 is provided with blade 26, through starting agitator 24, can drive blade 26 on the output shaft 25 and rotate in flocculation zone 6, the back of flocculation zone 6 is connected with water pipe 27, the back of water pipe 27 is connected with central water distribution pipe 28, the bottom of sedimentation tank 7 is connected with dredge 30, make the heavy under the bottom suspension mud of the bottom of oxidation bed through the gravity effect of sedimentation tank 7.
When the high-efficiency integrated sewage treatment equipment adopting the technical scheme is used, firstly, sewage is introduced into the first water distribution pipe 10 from the water inlet 8 of the integrated device, so that the sewage can uniformly enter the hydrolysis treatment tank 1, then, large particles and suspended matters in the sewage can be intercepted by the combined filler 11, the hydrolysis acidification efficiency is improved, then, the sewage above the hydrolysis treatment tank 1 flows into the decomposition tank 2 from the first water through holes 12 and finishes the denitrification process in the decomposition tank 2, secondly, the sewage flows into the aerobic zone 3 from the second water through holes 14, and oxygen can be continuously introduced into the aerobic zone 3 through the first aerator pipe 15, so that the organic pollutants adsorbed in the water can be conveniently ingested and decomposed by aerobic microorganisms, and then, the sewage can enter the separation zone 4 through the third water through holes 18, the up-flow solid-liquid separation module 19 is convenient for filtering pollutants again, so that separated gas can be discharged from the exhaust pipe 20, then sewage can enter the reaction zone 5 from the fourth water passing hole 21, after coagulation reaction is completed, the sewage flows into the flocculation zone 6 through the fifth water passing hole 22, the stirrer 24 is started, the blades 26 can be driven to rotate in the flocculation zone 6 through the output shaft 25, the sewage is convenient for flocculation, finally, the sewage can sequentially flow into the sedimentation tank 7 through the water pipe 27 and the central water distribution pipe 28, and suspended sludge with the specific gravity greater than that of water in the effluent of the contact oxidation bed is sunk to the bottom of the sedimentation tank 7 through the gravity effect, so that the sludge is discharged from the sludge discharge pipe 30, and good water quality is ensured to be output from the water outlet 9 of the integrated device.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (7)
1. The utility model provides a high-efficient integration sewage treatment device, includes hydrolysis treatment groove (1), its characterized in that: the right side of hydrolysis tank (1) is connected with decomposer (2), the right side of decomposer (2) is connected with good oxygen district (3), the right side of good oxygen district (3) is connected with separation district (4), the right side of separation district (4) is connected with reaction district (5), the right side of reaction district (5) is connected with flocculation zone (6), the right side of separation district (4) is connected with sedimentation tank (7), the left side of hydrolysis tank (1) is connected with integrated device water inlet (8), the right side of sedimentation tank (7) is connected with integrated device delivery port (9), the upper end of flocculation zone (6) is provided with first mount (23), the upper end of sedimentation tank (7) is provided with second mount (29).
2. The efficient integrated wastewater treatment device according to claim 1, wherein: the bottom of the hydrolysis treatment tank (1) is provided with a first water distribution pipe (10), the inner side of the hydrolysis treatment tank (1) is connected with a combined filler (11), and the right side of the hydrolysis treatment tank (1) is provided with a first water passing hole (12).
3. The efficient integrated wastewater treatment device according to claim 1, wherein: the bottom of decomposer (2) is installed second cloth water pipe (13), the right side of decomposer (2) is provided with second water hole (14).
4. The efficient integrated wastewater treatment device according to claim 1, wherein: the bottom of good oxygen district (3) is connected with first aeration pipe (15), the bottom of separation district (4) is connected with second aeration pipe (16), the upper end of first aeration pipe (15) and second aeration pipe (16) all is provided with micropore aeration head (17).
5. The efficient integrated wastewater treatment device according to claim 4, wherein: the right side of good oxygen district (3) is provided with third water hole (18), the inboard of separation district (4) is provided with up-flow solid-liquid separation module (19), the upper end of up-flow solid-liquid separation module (19) is connected with blast pipe (20), the right side of separation district (4) is provided with fourth water hole (21), the right side of reaction district (5) is provided with fifth water hole (22).
6. The efficient integrated wastewater treatment device according to claim 1, wherein: the upper end of first mount (23) is equipped with mixer (24), the lower extreme of mixer (24) is connected with output shaft (25), the surface of output shaft (25) is provided with blade (26).
7. The efficient integrated wastewater treatment device according to claim 1, wherein: the back of flocculation zone (6) is connected with water pipe (27), the back of water pipe (27) is connected with central water distribution pipe (28), the bottom of sedimentation tank (7) is connected with mud pipe (30).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321618752.5U CN220564445U (en) | 2023-06-25 | 2023-06-25 | High-efficient integration sewage treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321618752.5U CN220564445U (en) | 2023-06-25 | 2023-06-25 | High-efficient integration sewage treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220564445U true CN220564445U (en) | 2024-03-08 |
Family
ID=90088215
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321618752.5U Active CN220564445U (en) | 2023-06-25 | 2023-06-25 | High-efficient integration sewage treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220564445U (en) |
-
2023
- 2023-06-25 CN CN202321618752.5U patent/CN220564445U/en active Active
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