Super-magnetic loading sedimentation tank
By adding coagulants and magnetic seeds to the sludge loading sedimentation tank, the suspended particles are coagulated by the magnetic field, which solves the problem of low treatment efficiency of traditional sedimentation tanks and achieves a highly efficient water purification effect.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- JIANGSU XINGCHEN ENVIRONMENTAL PROTECTION GROUP
- Filing Date
- 2025-06-05
- Publication Date
- 2026-05-08
AI Technical Summary
Traditional sludge loading sedimentation tanks cannot quickly remove suspended solids and organic matter from wastewater, resulting in low treatment efficiency, poor effluent quality, increased floor space and operating costs.
The super magnetic loading sedimentation tank is used. By adding coagulants and magnetic seeds to the water, the magnetic field is used to make suspended particles and colloidal substances quickly coagulate into large particles, and the water is purified by sedimentation or filtration.
It achieves rapid sedimentation of suspended solids and organic matter, resulting in excellent effluent quality. The total phosphorus, suspended solids and turbidity indicators are superior to those of traditional processes, and the removal efficiency of non-dissolved COD is improved by more than 20%.
Smart Images

Figure CN224212478U_ABST
Abstract
Description
Technical Field
[0001] This utility model discloses a sedimentation tank, belonging to the technical field of sewage treatment equipment, specifically relating to a super magnetic loading sedimentation tank. Background Technology
[0002] The main function of a sludge loading sedimentation tank is to remove suspended solids and organic matter from wastewater. Simultaneously, through sludge thickening and recirculation, it maintains the activity and quantity of microorganisms in the biological treatment section. The sludge loading sedimentation tank removes suspended solids and organic matter from wastewater through gravity sedimentation. These suspended solids and organic matter mainly include denser solid particles and suspended organic matter, thereby reducing the organic load on subsequent biological treatment structures. However, wastewater contains various types of suspended solids and organic matter, and traditional sludge loading sedimentation tanks cannot quickly remove and treat them, resulting in low treatment efficiency, low effluent quality, increased land area, and higher operating costs. Utility Model Content
[0003] Purpose of the utility model: To provide a super magnetic loading sedimentation tank to solve the problems mentioned above.
[0004] Technical solution: A super magnetic loading sedimentation tank, a PAC stirring tank, a PAM stirring tank, a flocculation tank, a sludge scraping tank, a sludge buffer tank, and a sludge treatment tank;
[0005] The PAC mixing tank has an inlet pipe at its input end and an output end connected to the input end of the PAM mixing tank. The output end of the PAM mixing tank is connected to the input end of the flocculation tank. The sludge scraping tank is connected to the output end of the flocculation tank through a connecting pipe. The sludge buffer tank is connected to the sludge scraping tank.
[0006] The sludge treatment tank is equipped with a sludge return pump, a residual sludge pump and a sludge conveying pump. The sludge scraping tank is connected to the sludge return pump and the residual sludge pump. The sludge buffer tank is connected to the sludge conveying pump. The sludge return pump is connected to the PAM mixing tank.
[0007] In a further embodiment, a first flow hole is provided between the PAC mixing tank and the PAM mixing tank to connect the two, and a second flow hole is provided between the PAM mixing tank and the flocculation tank to connect the two.
[0008] In a further embodiment, the PAC mixing tank, the PAM mixing tank, and the flocculation tank are all equipped with a mixer and mixing blades.
[0009] In a further embodiment, the sludge scraper is provided in the sludge scraper tank and the upper part is provided with a triangular weir plate, and the connecting pipe is installed in the upper part of the flocculation tank and the sludge scraper tank.
[0010] In a further embodiment, a water outlet pipe is provided on the outside of the sludge scraping pool.
[0011] In a further embodiment, the bottom of the sludge scraping tank is connected to the input end of the sludge return pump via a first sludge pipe, and the output end of the sludge return pump is connected to the PAM mixing tank via a second sludge pipe.
[0012] In a further embodiment, a high-speed shear machine and a magnetic powder recovery machine are provided above the residual sludge pump. The input end of the magnetic powder recovery machine is connected to the first sludge pipe through a third sludge pipe, and the output end of the magnetic powder recovery machine is connected to the input of the high-speed shear machine. The output end of the high-speed shear machine is connected to the input end of the residual sludge pump through a fourth sludge pipe.
[0013] In a further embodiment, the input end of the sludge transport pump is connected to the sludge buffer tank through a fifth sludge pipe, and the output end of the sludge transport pump is connected to an external sludge tank through a sludge discharge pipe.
[0014] In a further embodiment, flow meters are provided on the second sludge pipe and the fourth sludge pipe.
[0015] In a further embodiment, a bypass pipe is provided between the flocculation tank and the sludge buffer tank.
[0016] Beneficial Effects: This novel super-magnetic loading sedimentation tank, by adding magnetic seeds and coagulants, utilizes the force of a magnetic field on charged particles to rapidly coagulate suspended particles and colloidal substances into larger particles, achieving water purification through sedimentation or filtration. This process significantly shortens coagulation and sedimentation time, achieving rapid settling and producing excellent effluent quality. Indicators such as total phosphorus (TP), suspended solids (SS), and turbidity are all superior to those of traditional processes. In particular, the removal efficiency of non-dissolved COD is more than 20% higher than that of conventional processes. Attached Figure Description
[0017] Figure 1 This is a plan view of the present invention.
[0018] Figure 2 This is a cross-sectional view (I-I) of this utility model.
[0019] Figure 3 This is a cross-sectional view (II-II) of this utility model.
[0020] Figure 4 This is a sectional view (III-III) of this utility model.
[0021] Figure 5 This is a cross-sectional view of the present invention along line IV-IV.
[0022] Attached reference numerals: 1. PAC mixing tank; 2. PAM mixing tank; 3. Flocculation tank; 4. Sludge scraper tank; 5. Sludge buffer tank; 6. Sludge treatment tank; 7. Inlet pipe; 8. Connecting pipe; 9. Sludge return pump; 10. Excess sludge pump; 11. Sludge transfer pump; 12. First overflow hole; 13. Second overflow hole; 14. Mixer; 15. Mixing blade; 16. Sludge scraper; 17. Triangular weir plate; 18. Outlet pipe; 19. First sludge pipe; 20. Second sludge pipe; 21. High shear machine; 22. Magnetic powder recovery machine; 23. Third sludge pipe; 24. Fourth sludge pipe; 25. Fifth sludge pipe; 26. Sludge discharge pipe; 27. Flow meter; 28. Overpass pipe. Detailed Implementation
[0023] The technical solution of this utility model will now be clearly and completely described with reference to the accompanying drawings. Obviously, the described embodiments are only some, not all, of the embodiments of this utility model. Based on the embodiments of this utility model, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of this utility model.
[0024] In the description of this utility model, it should be noted that the terms "center," "upper," "lower," "left," "right," "vertical," "horizontal," "inner," and "outer," etc., indicating the orientation or positional relationship, are based on the orientation or positional relationship shown in the accompanying drawings and are only for the convenience of describing this utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation, and therefore should not be construed as a limitation of this utility model. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and should not be construed as indicating or implying relative importance.
[0025] In the description of this utility model, it should be noted that, unless otherwise explicitly specified and limited, the terms "installation," "connection," and "joining" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; and they can refer to the internal connection of two components. Those skilled in the art can understand the specific meaning of the above terms in this utility model based on the specific circumstances. Furthermore, the technical features involved in the different embodiments of this utility model described below can be combined with each other as long as they do not conflict with each other.
[0026] A super magnetic loading sedimentation tank includes: a PAC stirring tank 1, a PAM stirring tank 2, a flocculation tank 3, a sludge scraping tank 4, a sludge buffer tank 5, and a sludge treatment tank 6.
[0027] In one embodiment, such as Figures 1 to 5As shown, the PAC mixing tank 1 has an inlet pipe 7 at its input end and its output end is connected to the input end of the PAM mixing tank 2. The output end of the PAM mixing tank 2 is connected to the input end of the flocculation tank 3. The sludge scraping tank 4 is connected to the output end of the flocculation tank 3 through a connecting pipe 8. The sludge buffer tank 5 is connected to the sludge scraping tank 4.
[0028] The sludge treatment tank 6 is equipped with a sludge return pump 9, a residual sludge pump 10 and a sludge conveying pump 11. The sludge scraping tank 4 is connected to the sludge return pump 9 and the residual sludge pump 10. The sludge buffer tank 5 is connected to the sludge conveying pump 11. The sludge return pump 9 is connected to the PAM mixing tank 2.
[0029] In one embodiment, such as Figures 1 to 5 As shown, a first flow hole 12 is provided between the PAC mixing tank 1 and the PAM mixing tank 2 to connect the two, and a second flow hole 13 is provided between the PAM mixing tank 2 and the flocculation tank 3 to connect the two.
[0030] In one embodiment, such as Figures 1 to 5 As shown, the PAC mixing tank 1, the PAM mixing tank 2 and the flocculation tank 3 are all equipped with a mixer 14 and a mixing blade 15.
[0031] In one embodiment, such as Figures 1 to 5 As shown, the sludge scraper 16 is provided in the sludge scraper tank 4, and the upper part is provided with a triangular weir plate 17. The connecting pipe 8 is installed in the upper part of the flocculation tank 3 and the sludge scraper tank 4.
[0032] In one embodiment, such as Figures 1 to 5 As shown, a water outlet pipe 18 is provided on the outside of the sludge scraping pool 4.
[0033] In one embodiment, such as Figures 1 to 5 As shown, the bottom of the sludge scraping tank 4 is connected to the input end of the sludge return pump 9 through the first sludge pipe 19, and the output end of the sludge return pump 9 is connected to the PAM mixing tank 2 through the second sludge pipe 20.
[0034] In one embodiment, such as Figures 1 to 5 As shown, a high-speed shear machine 21 and a magnetic powder recovery machine 22 are provided above the residual sludge pump 10. The input end of the magnetic powder recovery machine 22 is connected to the first sludge pipe 19 through the third sludge pipe 23. The output end of the magnetic powder recovery machine 22 is connected to the input of the high-speed shear machine 21. The output end of the high-speed shear machine 21 is connected to the input end of the residual sludge pump 10 through the fourth sludge pipe 24.
[0035] In one embodiment, such as Figures 1 to 5As shown, the input end of the sludge transport pump 11 is connected to the sludge buffer tank 5 through the fifth sludge pipe 25, and the output end of the sludge transport pump 11 is connected to the external sludge tank through the sludge discharge pipe 26.
[0036] In one embodiment, such as Figures 1 to 5 As shown, flow meters 27 are installed on the second sludge pipe 20 and the fourth sludge pipe 24.
[0037] In one embodiment, such as Figures 1 to 5 As shown, a bypass pipe 28 is provided between the flocculation tank 3 and the sludge buffer tank 5.
[0038] In one embodiment, such as Figures 1 to 5 As shown, the super-magnetic loading sedimentation tank induces a magnetic coagulation reaction by adding coagulants and magnetic seeds to the water, generating magnetic flocs. These flocs are adsorbed onto the continuously rotating permanent magnet disk and scraped off by magnetic scrapers, achieving solid-liquid separation. The treated water can be further processed through ecological treatment or disinfection, or discharged directly. The magnetic sludge is recycled through a magnetic powder recovery system, while the remaining sludge is sent to a sludge dewatering system for dewatering and off-site transportation.
[0039] Working Principle: When this invention is in operation, wastewater is first input into the PAC mixing tank 1 through the inlet pipe 7. Polyaluminum chloride (PAC) is added to the PAC mixing tank 1, and the mixture is stirred evenly by the mixer 14 and the stirring blades 15. The mixture then flows into the PAM mixing tank 2 through the first overflow hole 12. Polymer material (PAM) is added to the PAM mixing tank 2, and the mixture is stirred evenly by the mixer 14 and the stirring blades 15. The mixture then flows into the flocculation tank 3 through the second overflow hole 13. Flocculant is added to the flocculation tank 3, and the mixture is stirred evenly by the mixer 14 and the stirring blades 15. The mixture then flows through the connecting pipe 8. The sludge enters the sludge scraper tank 4, where it is moved to the lower part by the sludge scraper 16. Water flows out through the outlet pipe 18 at the upper part. When the flow rate is too large, it flows through the triangular weir plate 17 into the sludge buffer tank 5. At the same time, the sludge enters the sludge return pump 9 through the first sludge pipe 19. The sludge return pump 9 flows into the PAM sludge tank 2 through the second sludge pipe 20. Simultaneously, the sludge is passed through the magnetic powder recovery machine 22 and the high shear machine 21 through the third sludge pipe 23 and enters the residual sludge pump 10 through the fourth sludge pipe 24. The sludge transfer pump 11 connects to the sludge in the sludge buffer tank 5 through the fifth sludge pipe 25 and flows out through the sludge outlet pipe 26.
[0040] Obviously, the above embodiments are merely illustrative examples for clear explanation and are not intended to limit the implementation. Those skilled in the art will recognize that other variations or modifications can be made based on the above description. It is neither necessary nor possible to exhaustively list all possible implementations here. However, obvious variations or modifications derived therefrom are still within the protection scope of this invention.
Claims
1. A supermagnetically loaded sedimentation tank, characterized in that, include: PAC mixing tank, PAM mixing tank, flocculation tank, sludge scraping tank, sludge buffer tank and sludge treatment tank. The PAC mixing tank has an inlet pipe at its input end and an output end connected to the input end of the PAM mixing tank. The output end of the PAM mixing tank is connected to the input end of the flocculation tank. The sludge scraping tank is connected to the output end of the flocculation tank through a connecting pipe. The sludge buffer tank is connected to the sludge scraping tank. The sludge treatment tank is equipped with a sludge return pump, a residual sludge pump and a sludge conveying pump. The sludge scraping tank is connected to the sludge return pump and the residual sludge pump. The sludge buffer tank is connected to the sludge conveying pump. The sludge return pump is connected to the PAM mixing tank.
2. The supermagnetically loaded sedimentation tank according to claim 1, characterized in that, A first flow hole is provided between the PAC mixing tank and the PAM mixing tank to connect the two, and a second flow hole is provided between the PAM mixing tank and the flocculation tank to connect the two.
3. The supermagnetically loaded sedimentation tank according to claim 1, characterized in that, The PAC mixing tank, the PAM mixing tank, and the flocculation tank are all equipped with a mixer and mixing blades.
4. The supermagnetically loaded sedimentation tank according to claim 1, characterized in that, The sludge scraper is equipped with a sludge scraper and a triangular weir plate in the upper part. The connecting pipe is installed in the upper part of the flocculation tank and the sludge scraper.
5. The supermagnetically loaded sedimentation tank according to claim 1, characterized in that, The sludge scraper is equipped with a water outlet pipe on its outer side.
6. The supermagnetically loaded sedimentation tank according to claim 1, characterized in that, The bottom of the sludge scraping tank is connected to the input end of the sludge return pump via a first sludge pipe, and the output end of the sludge return pump is connected to the PAM mixing tank via a second sludge pipe.
7. The supermagnetically loaded sedimentation tank according to claim 6, characterized in that, Above the residual sludge pump are a high-speed shear machine and a magnetic powder recovery machine. The input end of the magnetic powder recovery machine is connected to the first sludge pipe through a third sludge pipe, and the output end of the magnetic powder recovery machine is connected to the input of the high-speed shear machine. The output end of the high-speed shear machine is connected to the input end of the residual sludge pump through a fourth sludge pipe.
8. The supermagnetically loaded sedimentation tank according to claim 1, characterized in that, The input end of the sludge transport pump is connected to the sludge buffer tank through the fifth sludge pipe, and the output end of the sludge transport pump is connected to the external sludge tank through the sludge discharge pipe.
9. The supermagnetically loaded sedimentation tank according to claim 7, characterized in that, The second sludge pipe and the fourth sludge pipe are equipped with flow meters.
10. The supermagnetically loaded sedimentation tank according to claim 1, characterized in that, An overpass pipe is provided between the flocculation tank and the sludge buffer tank.