A multi-stage rectification self-adaptive sedimentation treatment device for wastewater
Patent Information
- Application Number
- CN202611495260.X
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2026-09-24
- Publication Date
- 2026-10-30
AI Technical Summary
[0005]为此,本发明提供一种废水多级整流自适应沉淀处理装置,以解决现有技术中由于污泥刮除机构无法主动调整,而导致的刮除效果不好的问题
[0016]本发明通过将第二反应池与第一沉淀池串联,将两组沉淀处理串联到一起,并且沉淀池、絮凝池与反应池均是直接贴合到一起,通过开孔直接进行联通,减少土地占用率的同时,可以降低成本,且减少出现短流和死水区的情况,而通过设置结构相同且串联的两级反应-絮凝-沉淀单元(第一级和第二级),废水依次经历两次混合反应、絮凝和沉淀过程,实现了对废水的深度处理,有效去除了水中悬浮物及胶体杂质,出水水质显著提高,而在沉淀池中设置刮除推动组件,可针对沉淀池侧壁以及底板上的残留污泥进行刮除,还可以推动沉淀物到指定的出料位置,但是不同于现有技术的是设置了联动驱动组件,通过刮除推动组件本身的自旋转,进而驱动联动驱动组件产生电能,这个电能为交流电,利用交流电的周期特性,驱动刮除结构周期性伸出与收回,而且旋转运动也在进行,在自动调节的情况下,实现刮除与推料两种运动,且不需要额外驱动源,降低能量消耗的同时,无需浪费额外时间清理沉淀池,提高污水处理时间。
Smart Images

Figure CN123002995A_ABST
Abstract
Description
Technical Field
[0001] This invention relates to the field of wastewater treatment technology, specifically to a multi-stage rectifier adaptive sedimentation treatment device for wastewater. Background Technology
[0002] In wastewater treatment engineering, sedimentation separation is the core process for removing suspended solids and colloidal impurities from water, and its operational efficiency directly affects the load of subsequent advanced treatment units and the final effluent quality.
[0003] Existing sedimentation treatment systems mostly adopt a split layout, where the reaction tank, flocculation tank, and sedimentation tank are independent and connected by pipes or channels. This layout not only occupies a large area, increasing the investment cost of civil engineering and piping, but more importantly, the connecting pipes between units are prone to head loss and water flow turbulence, resulting in uneven water flow distribution into the sedimentation tank, short-circuiting, and dead water zones. This significantly reduces the effective volume utilization rate of the sedimentation tank and affects the overall treatment effect. After long-term operation, a large amount of concentrated sludge accumulates at the bottom of the sedimentation tank. If sludge removal is not timely or thorough, it will float to the surface due to anaerobic fermentation, affecting the effluent quality. Existing sludge removal equipment often only effectively cleans the central area of the tank bottom, making it difficult to reach the four corners of the sedimentation tank and the sludge adhering to the tank wall surface. These corner dead zones and tank wall sludge, if left to stagnate for a long time, will gradually harden and compact, not only reducing the effective sedimentation volume but also increasing the difficulty of subsequent cleaning. In severe cases, it may require shutdown for manual cleaning, greatly increasing operation and maintenance costs and workload. In addition, although some improved devices are equipped with sludge scrapers, their scraper blades are usually of a fixed radial length and cannot adaptively conform to the shape of the pool wall at different locations. For sedimentation tanks with curved walls or irregular structures, the scraping effect is even worse.
[0004] Therefore, how to provide a multi-stage rectified adaptive sedimentation treatment device for wastewater to solve the defects of existing sewage sedimentation treatment structures is a technical problem that urgently needs to be solved by those skilled in the art. Summary of the Invention
[0005] To address this issue, the present invention provides a multi-stage rectifier adaptive sedimentation treatment device for wastewater, which solves the problem of poor sludge removal effect caused by the inability of the sludge scraping mechanism to actively adjust in the prior art.
[0006] To achieve the above objectives, the present invention provides the following technical solution: This invention discloses a multi-stage rectification adaptive sedimentation treatment device for wastewater, comprising: Several first reaction tanks are arranged side by side and are interconnected. The first flocculation tank is installed behind the first reaction tank. A first sedimentation tank is provided on the left side of the first flocculation tank and the first reaction tank. The front end of the first flocculation tank is connected to the first reaction tank, and the left side of the first flocculation tank is connected to the first sedimentation tank. Several second reaction tanks are arranged side by side and installed behind the first sedimentation tank. A second flocculation tank is arranged behind the second reaction tank, and the second reaction tank and the second flocculation tank are connected. The second sedimentation tank is located to the right of the second flocculation tank, and the second sedimentation tank is connected to the second flocculation tank. The mixing components are arranged in pairs and installed above the first reaction tank and the second reaction tank, respectively. The flocculation mixing components are arranged in pairs and installed above the first flocculation tank and the second flocculation tank respectively; A scraping and pushing component is installed above the first sedimentation tank and the second sedimentation tank; the first sedimentation tank and the second sedimentation tank are equipped with several inclined filter plates and several filter outlet tanks. A linkage drive component is installed in the scraping push component; The first reaction tank, the first flocculation tank, and the first sedimentation tank have the same structure as the second reaction tank, the second flocculation tank, and the second sedimentation tank, respectively.
[0007] In one possible implementation, a connecting groove is formed on the side wall of the first reaction tank, and the two first reaction tanks are connected by the connecting groove. A water passage hole is formed at the bottom of the side wall of the first reaction tank, and the first reaction tank is connected to the first flocculation tank by the water passage hole.
[0008] In one possible implementation, the first flocculation tank has a through groove on its side wall, and the first flocculation tank is connected to the first sedimentation tank through the through groove. The bottom of the first flocculation tank has a round hole.
[0009] In one possible implementation, a baffle is installed on the bottom plate of the first sedimentation tank. An inclined plate is installed between one end of the baffle and the bottom plate of the first sedimentation tank. An annular slope is provided on the bottom plate of the first sedimentation tank between the other end of the inclined plate and the side plate of the first sedimentation tank. A frustum-shaped storage groove is also opened on the bottom plate of the first sedimentation tank. The frustum-shaped storage groove is located below the annular slope. Several arc-shaped walls are provided on the inclined plate and the side plate wall of the first sedimentation tank. The arc-shaped walls are located above the annular slope. A guide plate is provided between the two side walls of the first sedimentation tank. The guide plate is parallel to the baffle.
[0010] In one possible implementation, the hybrid component includes: A placement plate is installed on top of several first reaction tanks, and several first rotary motors are installed on the top of the placement plate; A drive rod is installed at the bottom output end of the first rotary motor. The bottom of the drive rod passes through the placement plate, and several rotating disks are installed on the drive rod. Several conical teeth are installed at the bottom of the rotating disk.
[0011] In one possible implementation, the flocculation and stirring assembly includes: A connecting plate is installed above the first or second flocculation tank. A second rotary motor is installed on the top of the connecting plate, and a rotary shaft is installed at the bottom output end of the second rotary motor, with the bottom of the rotary shaft extending out of the connecting plate. Several connecting plates are installed on the side wall of the first flocculation tank; An annular guide barrel is installed between several of the connecting plates; Several toothed plates are installed on the bottom periphery of the rotating shaft.
[0012] In one possible implementation, the scraping actuation component includes: The mounting plate has an internal mounting groove. The mounting plate is installed on the top of the first sedimentation tank or the second sedimentation tank. A drive motor is installed on the top of the mounting plate. A first gear and a second gear are installed in the mounting groove. The first gear and the second gear mesh. The first gear is installed at the bottom output end of the drive motor. A limit sleeve is installed at the bottom of the mounting plate. The bushing is installed at the bottom of the frustum-shaped storage slot; The rotating shaft is mounted at the top in the second gear, and at the bottom, it passes through the bottom plate of the mounting plate and the limiting sleeve and is inserted into the bushing. Several trapezoidal plates are installed on the bottom periphery of the rotating shaft, and the trapezoidal plates are disposed in the frustum-shaped storage groove; An annular sleeve is installed on the rotating shaft. The annular sleeve is positioned above the trapezoidal plate. Several sleeves are provided on the outer periphery of the annular sleeve, and an annular scraper is installed at the bottom of the sleeve. An I-shaped slide rod is slidably connected in the sleeve. A connecting rod is installed at the outer end of the I-shaped slide rod, and a first scraper is installed at the outer end of the connecting rod. The first scraper has arc-shaped surfaces at both ends. A drive rack is symmetrically arranged on the side of the middle part of the I-shaped slide rod, and a permanent magnet is provided on the inner end surface of the I-shaped slide rod. The linkage component is connected at its upper end to the I-shaped slide bar, and a second scraper is connected at the bottom of the linkage component.
[0013] In one possible implementation, the linkage component includes: T-shaped connecting cylinders are arranged in pairs, with their tops mounted on the inner wall of the top of the sleeve. A linkage gear is rotatably connected to the bottom of the T-shaped connecting cylinder. An internal thread groove is opened at the center of the linkage gear, and the linkage gear meshes with the drive rack. The threaded lifting rods are installed in pairs and screwed into the two internal threaded grooves. A crossbar is connected at both ends to the bottom of the two threaded lifting rods. A connecting rod is installed at the bottom of the crossbar. The bottom of the connecting rod passes through the sleeve and the annular scraper head, and a second scraper is installed at the end.
[0014] In one possible implementation, several rectangular grooves are formed on the upper sidewall of the rotating shaft; The linkage drive component includes: An anisotropic magnet is installed on the inner side of the bottom of the limiting sleeve; Several coils are arranged in the rotating shaft, with a portion of one coil passing through two symmetrical rectangular slots, and an energized coil is installed between the two ends of the coil. An electromagnet is installed in the rotating shaft, with both ends of the electromagnet extending out of the rotating shaft and facing the permanent magnet. The coil is located outside the electromagnet.
[0015] In one possible implementation, a T-shaped pipe is provided at the bottom of the first flocculation tank, the first sedimentation tank, the second flocculation tank, and the second sedimentation tank. One end of the T-shaped pipe extends into the first sedimentation tank or the second sedimentation tank, and the other end of the T-shaped pipe is located on the outermost side. A section of the T-shaped pipe is also located in the first flocculation tank or the second flocculation tank.
[0016] This invention connects two sedimentation treatment systems in series, with the second reaction tank and the first sedimentation tank connected together. The sedimentation tank, flocculation tank, and reaction tank are all directly attached together and connected via openings. This reduces land occupation, lowers costs, and minimizes short-circuiting and stagnant water zones. By setting up two identical, series-connected reaction-flocculation-sedimentation units (first and second stages), wastewater undergoes two sequential mixing, flocculation, and sedimentation processes, achieving deep wastewater treatment. This effectively removes suspended solids and colloidal impurities, significantly improving effluent quality. A scraper is installed in the sedimentation tank to drive... This component can scrape off residual sludge on the side walls and bottom plate of the sedimentation tank and push the sediment to the designated discharge position. However, unlike existing technologies, it is equipped with a linkage drive component. The scraping component itself rotates, which in turn drives the linkage drive component to generate electrical energy. This electrical energy is alternating current. Utilizing the periodic characteristics of alternating current, the scraping structure is periodically extended and retracted, and the rotational motion is also in progress. With automatic adjustment, it realizes both scraping and pushing movements, without the need for an additional drive source. This reduces energy consumption and eliminates the need to waste extra time cleaning the sedimentation tank, thereby improving wastewater treatment time. Attached Figure Description
[0017] To more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings described below are merely exemplary, and those skilled in the art can derive other embodiments based on the provided drawings without creative effort.
[0018] The structures, proportions, sizes, etc. illustrated in this specification are only for the purpose of assisting those skilled in the art in understanding and reading the content disclosed herein, and are not intended to limit the conditions under which the present invention can be implemented. Therefore, they have no substantial technical significance. Any modifications to the structure, changes in the proportions, or adjustments to the size, without affecting the effects and objectives that the present invention can produce, should still fall within the scope of the technical content disclosed in the present invention.
[0019] Figure 1 A perspective view of the multi-stage rectification adaptive sedimentation treatment device for wastewater provided by the present invention; Figure 2 Cross-sectional view of the filter outlet tank and filter inclined plate provided by the present invention; Figure 3 A cross-sectional view of the first reaction tank provided for this invention; Figure 4 A cross-sectional view of the first flocculation tank provided by the present invention; Figure 5 A cross-sectional view of the first sedimentation tank provided for this invention; Figure 6 A perspective view of the hybrid component provided by the present invention; Figure 7 A cross-sectional view of the flocculation stirring assembly provided by the present invention; Figure 8 A perspective view of the scraping and pushing component provided by the present invention; Figure 9 A cross-sectional view of the scraping and pushing component provided by the present invention; Figure 10 Provided by the present invention Figure 9 Enlarged view of a portion of point A in the middle; Figure 11 A cross-sectional view of the rotating shaft provided by the present invention; Figure 12 Provided by the present invention Figure 11 Enlarged view of a section at point B in the middle; Figure 13 Provided by the present invention Figure 11 Enlarged view of a section at point C; Figure 14 A cross-sectional view of a T-shaped pipeline provided by the present invention; In the diagram: 1 Second sedimentation tank; 2 Scraper pushing assembly; 21 Drive motor; 22 First gear; 23 Second gear; 24 Mounting plate; 25 Limiting sleeve; 26 Rotating shaft; 27 First scraper; 28 Sleeve; 29 Annular sleeve; 210 Trapezoidal plate; 211 Bushing; 212 Second scraper; 214 Connecting rod; 215 I-shaped slide bar; 216 Linkage component; 2161 T-shaped connecting cylinder; 2162 Threaded lifting rod; 2163 Connecting rod; 2164 Crossbar; 2165 Linkage gear; 217 Drive rack; 218 Permanent magnet; 219 Annular scraper head; 3 Filter outlet tank; 4 Filter inclined plate; 5 First reaction tank; 51 Connecting tank; 52 Water passage hole; 6 Mixing component; 61 First rotary motor; 62 Placement plate; 63 Drive rod; 64 Rotary disk; 65 Conical tooth; 7 Flocculation stirring component; 71 Connecting plate; 72 Second rotary motor; 73 Annular guide tank; 74 Connecting plate; 75 Rotating shaft; 76 Toothed plate; 8 First sedimentation tank; 81 Baffle; 82 Inclined plate; 83 Annular slope; 84 Frustum-shaped receiving trough; 85 Arc wall; 86 Guide plate; 9 First flocculation tank; 91 Circular hole; 92 Through groove; 10 Second reaction tank; 20 Second flocculation tank; 30 Linkage drive component; 301 Opposite magnet; 302 Coil; 303 Electromagnet; 304 Energized coil; 40 T-type pipeline. Detailed Implementation
[0020] The following specific embodiments illustrate the implementation of the present invention. Those skilled in the art can easily understand other advantages and effects of the present invention from the content disclosed in this specification. Obviously, the described embodiments are only some, not all, of the embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of the present invention.
[0021] Please refer to Figures 1-14 The present invention discloses a multi-stage rectification adaptive sedimentation treatment device for wastewater, such as... Figures 1-2 The system includes a second sedimentation tank 1, a scraping and pushing assembly 2, a filter outlet tank 3, a filter inclined plate 4, a first reaction tank 5, a mixing assembly 6, a flocculation and stirring assembly 7, a first sedimentation tank 8, a first flocculation tank 9, a second reaction tank 10, a second flocculation tank 20, and a linkage drive assembly 30. Several first reaction tanks 5 are arranged side-by-side and interconnected. The first flocculation tank 9 is installed behind the first reaction tank 5. A first sedimentation tank 8 is located to the left of the first flocculation tank 9 and the first reaction tank 5. The front end of the first flocculation tank 9 is connected to the first reaction tank 5, and its left side is connected to the first sedimentation tank 8. Several second reaction tanks 10 are arranged side-by-side and installed behind the first sedimentation tank 8. A second flocculation tank 20 is located behind the second reaction tank 10. The second reaction tank 1... The first reaction tank 5 and the second reaction tank 10 are connected. The second sedimentation tank 1 is located on the right side of the second flocculation tank 20. The second sedimentation tank 1 is connected to the second flocculation tank 20. The mixing components 6 are arranged in pairs and installed above the first reaction tank 5 and the second reaction tank 10 respectively. The flocculation stirring components 7 are arranged in pairs and installed above the first flocculation tank 9 and the second flocculation tank 20 respectively. The scraping and pushing components 2 are installed above the first sedimentation tank 8 and the second sedimentation tank 1. Several filter inclined plates 4 and several filter outlet tanks 3 are installed inside the first sedimentation tank 8 and the second sedimentation tank 1. The linkage drive component 30 is installed in the scraping and pushing components 2. The first reaction tank 5, the first flocculation tank 9, and the first sedimentation tank 8 have the same structure as the second reaction tank 10, the second flocculation tank 20, and the second sedimentation tank 1 respectively. Two sets of sedimentation devices are used to achieve secondary purification of sewage and improve water treatment efficiency. The scraping and pushing component 2, the mixing component 6 and the flocculation and stirring component 7 agitate the water and accelerate sedimentation. The filter inclined plate 4 blocks the flocs and allows the purified water to flow through. The purified water is discharged through the filter outlet tank 3. It should be noted that the purified water in the first sedimentation tank 8 enters the second reaction tank 10 through the filter outlet tank 3. The water inlet of the filter outlet tank 3 enters through the side wall and flows out from both ends. The side wall of the filter outlet tank 3 has a serrated structure to block large particles and prevent them from entering the next stage of the reaction tank.
[0022] In a specific embodiment, such as Figure 3The first reaction tank 5 has a connecting groove 51 on its side wall, which connects two first reaction tanks 5. A water passage hole 52 is opened at the bottom of the side wall of the first reaction tank 5, which connects the first reaction tank 5 to the first flocculation tank 9. Since several first reaction tanks 5 are connected in series, the connecting groove 51 is needed to ensure that the water levels in the first reaction tanks 5 are equal. The water passage hole 52 is used to allow water from the first reaction tank 5 to enter the first flocculation tank 9.
[0023] In a specific embodiment, such as Figure 4 The first flocculation tank 9 has a through groove 92 on its side wall, which connects the first flocculation tank 9 to the first sedimentation tank 8. The bottom of the first flocculation tank 9 has a round hole 91. The through groove 92 is used to connect the first sedimentation tank 8, while the round hole 91 is used to install the T-shaped pipe 40 to allow the sludge sediment to be returned.
[0024] In a specific embodiment, such as Figure 5 A baffle 81 is installed on the bottom plate of the first sedimentation tank 8. An inclined plate 82 is installed between one end of the baffle 81 and the bottom plate of the first sedimentation tank 8. An annular ramp 83 is provided on the bottom plate of the first sedimentation tank 8 between the other end of the inclined plate 82 and the side plate of the first sedimentation tank 8. A frustum-shaped storage trough 84 is also opened on the bottom plate of the first sedimentation tank 8. The frustum-shaped storage trough 84 is located below the annular ramp 83. Several arc-shaped walls 85 are provided on the inclined plate 82 and the side plate wall of the first sedimentation tank 8. The arc-shaped walls 85 are located above the annular ramp 83. A guide plate 86 is provided between the two side walls of the first sedimentation tank 8. The guide plate 86 is parallel to the baffle 81. By setting baffle 81, the flow path of flocs is increased, allowing more sewage to mix with chemicals to produce flocs. Inclined plate 82 is used to guide the flocs and prevent them from falling to the bottom of baffle 81 and forming sludge. Guide plate 86 is used to guide the flow of water. Annular slope 83 is used to allow the sludge formed by floc sedimentation to fall into frustum-shaped collection tank 84. Arc wall 85 is used to guide the flow of sludge.
[0025] In a specific embodiment, such as Figure 6 The mixing component 6 includes a first rotary motor 61, a placement plate 62, a drive rod 63, a rotating disk 64, and conical teeth 65. The placement plate 62 is installed on top of several first reaction tanks 5, and several first rotary motors 61 are mounted on the top of the placement plate 62. The drive rod 63 is installed at the bottom output end of the first rotary motors 61, and its bottom passes through the placement plate 62. Several rotating disks 64 are mounted on the drive rod 63, and several conical teeth 65 are installed at the bottom of the rotating disks 64. When the first rotary motor 61 is started, the drive rod 63 drives the rotating disks 64 and conical teeth 65 to rotate at high speed, which vigorously stirs and mixes the wastewater with the added agents (such as coagulants) to form fine flocs.
[0026] In a specific embodiment, such as Figure 7 The flocculation and stirring assembly 7 includes a connecting plate 71, a second rotary motor 72, an annular guide barrel 73, connecting plates 74, a rotating shaft 75, and toothed plates 76. The connecting plate 71 is installed above the first flocculation tank 9 or the second flocculation tank 20. The second rotary motor 72 is installed on top of the connecting plate 71, and a rotating shaft 75 is installed at the bottom output end of the second rotary motor 72. The bottom of the rotating shaft 75 extends out of the connecting plate 71. Several connecting plates 74 are installed on the side wall of the first flocculation tank 9. The annular guide barrel 73 is installed between the several connecting plates 74, and several toothed plates 76 are installed on the bottom periphery of the rotating shaft 75. The annular guide barrel 73, installed between the several connecting plates 74, forms an annular guiding space, allowing the water flow in the flocculation tank to circulate and promoting floc collision. When the second rotary motor 72 drives the rotating shaft 75 to rotate, the toothed plates 76 rotate accordingly, gently stirring the wastewater and helping small flocs grow into larger flocs. At the same time, the annular guide barrel 73 restricts the water flow path, preventing turbulence from damaging the flocs.
[0027] In a specific embodiment, such as Figures 8-9 The scraping and pushing assembly 2 includes a drive motor 21, a first gear 22, a second gear 23, a mounting plate 24, a limiting sleeve 25, a rotating shaft 26, a first scraper 27, a sleeve 28, an annular sleeve 29, a trapezoidal plate 210, a bushing 211, a second scraper 212, a connecting rod 214, an I-shaped slide rod 215, a linkage component 216, a drive rack 217, a permanent magnet 218, and an annular scraper head 219. The mounting plate 24 has an internal mounting groove and is mounted on the top of the first sedimentation tank 8 or the second sedimentation tank 1. The drive motor 21 is mounted on the top of the mounting plate 24. The first gear 22 and the second gear 23 are installed in the mounting groove and mesh with each other. The first gear 22 is mounted on the bottom output end of the drive motor 21. The limiting sleeve 25 is mounted on the bottom of the mounting plate 24. The bushing 211 is mounted on the bottom of the frustum-shaped receiving groove 84. The top of the rotating shaft 26 is mounted in the second gear 23. The bottom of the rotating shaft 26 passes through the base plate of the mounting plate 24 and the limiting sleeve 25, and is inserted into the bushing 211. Several trapezoidal plates 210 are installed on the bottom periphery of the rotating shaft 26. The trapezoidal plates 210 are set in the frustum-shaped storage groove 84. The annular sleeve 29 is installed on the rotating shaft 26 and is positioned above the trapezoidal plates 210. Several sleeves 28 are provided on the outer periphery of the annular sleeve 29. An annular scraper 219 is installed at the bottom of the sleeve 28. I-shaped slide rod 2 15 is slidably connected in sleeve 28. A connecting rod 214 is installed on the outer end of the I-shaped slide rod 215. A first scraper 27 is installed on the outer end of the connecting rod 214. The first scraper 27 has arc-shaped surfaces at both ends. A drive rack 217 is symmetrically arranged on the side of the middle part of the I-shaped slide rod 215. A permanent magnet 218 is provided on the inner end surface of the I-shaped slide rod 215. The upper end of the linkage component 216 is connected to the I-shaped slide rod 215. A second scraper 212 is connected to the bottom of the linkage component 216.
[0028] In this embodiment, the drive motor 21 drives the first gear 22 to rotate. The first gear 22 is a small gear, while the second gear 23 is a large gear. The small gear drives the large gear to achieve deceleration, because low-speed stirring is required during sedimentation. If the stirring is too fast, the sediment will be sent back to the flocculation tank. The rotation of the second gear 23 causes the rotating shaft 26 to rotate. The limiting sleeve 25 is a fixing component installed at the bottom of the mounting plate 24. An anisotropic magnet 301 is installed in the limiting sleeve 25. The rotation of the rotating shaft 26 will drive the annular sleeve 29 to rotate, which will eventually cause the sleeve 28 to rotate. The rotation of the sleeve 28 will cause the first scraper 27 and the second scraper 212 to rotate synchronously, thereby agitating the sediment. The trapezoidal plate 210 is used to agitate the sludge formed by sedimentation in the frustum-shaped collection tank 84, preventing the sludge from solidifying in the frustum-shaped collection tank 84. At the same time, the eddy current formed by the rotation will carry the sludge into the T-shaped pipe 40. The bushing 211 is used to stabilize the rotation of the rotating shaft 26 and prevent it from deviating.
[0029] In a specific embodiment, such as Figure 10The linkage component 216 includes a T-shaped connecting cylinder 2161, a threaded lifting rod 2162, a connecting rod 2163, a crossbar 2164, and a linkage gear 2165. The T-shaped connecting cylinders 2161 are arranged in pairs, with their tops installed on the inner wall of the top of the sleeve 28. The bottom of the T-shaped connecting cylinder 2161 is rotatably connected to the linkage gear 2165. The linkage gear 2165 has an internal thread groove at its center and meshes with the drive rack 217. The threaded lifting rods 2162 are arranged in pairs and are screwed into the two internal thread grooves. The two ends of the crossbar 2164 are connected to the bottom of the two threaded lifting rods 2162. The bottom of the crossbar 2164 is equipped with a connecting rod 2163. The bottom of the connecting rod 2163 passes through the sleeve 28 and the annular scraper head 219, and a second scraper 212 is installed at its end. The linkage component 216 is used to control the movement of the second scraper 212. Through the displacement of the I-shaped slide bar 215, the drive rack 217 causes the linkage gear 2165 to rotate at the bottom of the T-shaped connecting cylinder 2161. The internal thread structure of the linkage gear 2165 drives the threaded lifting rod 2162 to move vertically. The threaded lifting rod 2162 then moves the crossbar 2164, which in turn moves the connecting rod 2163 up and down. This causes the second scraper 212 to either conform to or move away from the annular ramp 83, achieving both pushing and scraping movements. It is important to note that during the outward movement of the I-shaped slide bar 215, the crossbar 2164 moves upward, meaning that sludge is first removed from the sidewall. After scraping, the second scraper 212 moves downward to scrape material from the annular ramp 83, preventing the formation of sludge. In cases of secondary bonding or sludge falling onto the second scraper 212, it is important to note that the lifting and lowering movement of the threaded lifting rod 2162 will not affect the movement of the I-shaped slide rod 215. All movements are driven by the linkage drive assembly 30 to prevent errors in movement. The annular scraper head 219 is used to scrape water off the connecting rod 2163 to prevent water from entering the sleeve 28. At the same time, the tapered shape at the outer end of the sleeve 28 also achieves the water scraping effect. The I-shaped slide rod 215 is I-shaped, and its wide structure at both ends prevents water from entering the annular sleeve 29. Even if water does enter the annular sleeve 29, only the electromagnet 303 protrudes from the side of the rotating shaft 26. As long as the protruding end of the electromagnet 303 is welded to the rotating shaft 26, water cannot enter the inner side of the rotating shaft 26, thus not affecting the operation of the linkage drive assembly 30, extending its service life, and preventing water pollution.
[0030] In a specific embodiment, such as Figures 11-13The upper side wall of the rotating shaft 26 has several rectangular slots. The linkage drive assembly 30 includes an anisotropic magnet 301, a coil 302, an electromagnet 303, and an energized coil 304. The anisotropic magnet 301 is installed inside the bottom of the limiting sleeve 25. Several coils 302 are arranged in the rotating shaft 26. A portion of one coil 302 passes through two symmetrical rectangular slots. An energized coil 304 is installed between the two ends of the coil 302. The electromagnet 303 is installed in the rotating shaft 26. Both ends of the electromagnet 303 pass through the rotating shaft 26. The two ends of the electromagnet 303 face the permanent magnet 218. The coil 302 is arranged outside the electromagnet 303. A coil 302 passes through the rectangular slot. The coil 302, being rectangular in shape, sweeps across the opposite magnet 301, conforming to the principle of a generator where a looped conductor cuts magnetic field lines, causing a current to flow through the coil 302. This current causes the electromagnet 303 to become magnetic. The principle behind this current generation is the same as that of an AC generator, satisfying Em=NBSω. Since the rotational angular velocity ω of the rotating shaft 26 is small, and the energized coil 304 has a certain resistance, the current generated by the coil 302 is small and will not cause a short circuit. The magnetism of the electromagnet 303 begins to drive the permanent magnet 218 to shift. It is important to note that two types of magnetism are generated at the two ends of the electromagnet 303. There are two methods for 218. One is that the permanent magnets 218 at both ends use the same magnetism. In this way, only one end of the I-shaped slide rod 215 is in an outward movement state, carrying the first scraper 27 to scrape the side wall. The first scraper 27 has an arc-shaped structure at both ends, which is used to scrape the mud at the corner. The other method is that the permanent magnets 218 at both ends use opposite magnets to realize the synchronous movement of the I-shaped slide rods 215 at both ends, realizing synchronous scraping at both ends. Since the coil 302 generates alternating current, the magnetic pole direction of the electromagnet 303 will change periodically, thereby driving the permanent magnet 218 to drive the I-shaped slide rod 215 to reciprocate in the sleeve 28, realizing the periodic scraping of the side wall by the first scraper 27.
[0031] In a specific embodiment, such as Figure 14 T-shaped pipes 40 are installed at the bottom of the first flocculation tank 9, the first sedimentation tank 8, the second flocculation tank 20, and the second sedimentation tank 1. One end of the T-shaped pipe 40 extends into the first sedimentation tank 8 or the second sedimentation tank 1, and the other end is located on the outermost side. A section of the T-shaped pipe 40 is also installed in the first flocculation tank 9 or the second flocculation tank 20. The T-shaped pipes 40 are used to return the sediment to the flocculation tanks for secondary use, while the remaining sludge is discharged through the T-shaped pipes 40.
[0032] When using this invention, as Figure 1As shown, wastewater flows into one of the first reaction tanks 5 through the inlet pipe on the side of the first reaction tank 5, and then through the connecting channel 51 to fill all three first reaction tanks 5. During the filling process, reaction reagents such as lime, calcium chloride, or PAC are added. At the same time as the wastewater is added, the mixing component 6 is started. After the reaction reagents are added, the high-speed stirring of the mixing component 6 mixes the reaction reagents and wastewater evenly and completes the destabilization of colloids. The mixed fluid enters the first flocculation tank 9 through the water passage 52. PAM coagulant is added to the first flocculation tank 9, and then the flocculation stirring component 7 stirs at low speed to form dense large flocs. The flocs are carried by the water and flow into the first sedimentation tank 8 through the channel 92. The filter inclined plate 4 blocks the flocs, and the flocs are intercepted by the filter inclined plate 4 and settle to the bottom of the first sedimentation tank 8. The scraping and pushing component 2 removes the flocs. The sediment is stirred and settled, and finally pushed into the frustum-shaped collection tank 84 by the scraping and pushing component 2. At the same time, the scraping and pushing component 2 also scrapes away the residual sediment on the side wall and bottom plate of the first sedimentation tank 8 to prevent sludge from adhering and causing problems such as reduced volume and difficulty in cleaning. The side wall of the first reaction tank 5 is also opened with a water inlet hole, which is connected to the output end of the filter outlet tank 3 in the first sedimentation tank 8. The water will then enter the second reaction tank 10 through the filter outlet tank 3. In the second reaction tank 10, reaction reagents such as lime, calcium chloride or PAC are added to carry out secondary reaction. The water after reaction enters the second flocculation tank 20. In the second flocculation tank 20, PAM coagulant is added to carry out secondary flocculation. Finally, secondary sedimentation is completed in the second sedimentation tank 1, making the sewage cleaner. Through multi-stage sedimentation treatment, the sewage treatment efficiency is significantly improved.
[0033] Traditional equipment for sedimentation and sludge removal connects the second scraper 212 to a hydraulic system. Hydraulic oil is supplied to drive the scraper 212 downwards, scraping away sludge from the bottom of the sedimentation tank. However, using a hydraulic system requires a hydraulic cylinder and pump. The hydraulic cylinder is often submerged in the water, necessitating pipelines to transport the hydraulic oil. Hydraulic pumps are typically electrically controlled, requiring them to be located outside the water body and connected via pipelines. This not only increases costs but also requires large quantities of hydraulic oil. Furthermore, the pipelines, constantly immersed in sewage and chemicals, are prone to corrosion and leaks, which can pollute the water and defeat the purpose of wastewater treatment. In this structure, the hydraulic pump is mounted on the rotating shaft 26, affecting its rotation. Existing devices also lack a structure for removing sludge from the side walls of the sedimentation tank, leading to reduced sedimentation volume and increased cleaning difficulty. To address the aforementioned problem, this structure incorporates a linkage drive assembly 30. A drive motor 21 rotates the rotating shaft 26. A magnet 301 of a different shape is housed within the limiting sleeve 25. The rotation of the rotating shaft 26 causes the coil 302 within it to rotate as well. As the coil 302 rotates, it sweeps across the magnet 301, generating a cutting motion of magnetic field lines. Based on the principle of magnetism generating electricity, a current is generated in the coil 302 when it sweeps across it. This current causes the electromagnet 303 to become magnetic, driving the permanent magnet. The 218 carries the I-shaped slide bar 215 and reciprocates along the sleeve 28, while the rotating shaft 26 carries the annular scraper head 219 and rotates in the sedimentation tank. In this way, the sludge scraping operation on the inner wall of the sedimentation tank can be realized. The I-shaped slide bar 215 also drives the linkage component 216 to move, so that the second scraper 212 moves up and down, realizing the conveying of scraped sludge and the scraping operation on the bottom surface of the sedimentation tank. Moreover, the transmission structure is not set in the water and does not add an additional drive source, saving costs while ensuring that there are no impurities in the water.
[0034] Although the present invention has been described in detail above with general descriptions and specific embodiments, modifications or improvements can be made to it, which will be obvious to those skilled in the art. Therefore, all such modifications or improvements made without departing from the spirit of the present invention fall within the scope of protection claimed by the present invention.
Claims
1. A multi-stage rectification adaptive sedimentation treatment device for wastewater, characterized in that, include: Several first reaction tanks (5) are arranged side by side and interconnected. The first flocculation tank (9) is installed behind the first reaction tank (5). The first flocculation tank (9) and the first reaction tank (5) are provided with a first sedimentation tank (8) on the left side. The front end of the first flocculation tank (9) is connected to the first reaction tank (5), and the left side of the first flocculation tank (9) is connected to the first sedimentation tank (8). Several second reaction tanks (10) are arranged side by side and installed behind the first sedimentation tank (8). A second flocculation tank (20) is arranged behind the second reaction tank (10). The second reaction tank (10) and the second flocculation tank (20) are connected. The second sedimentation tank (1) is located on the right side of the second flocculation tank (20), and the second sedimentation tank (1) is connected to the second flocculation tank (20); The mixing components (6) are arranged in pairs and installed above the first reaction tank (5) and the second reaction tank (10) respectively; The flocculation stirring components (7) are arranged in pairs and installed above the first flocculation tank (9) and the second flocculation tank (20) respectively; The scraping and pushing component (2) is installed above the first sedimentation tank (8) and the second sedimentation tank (1); the first sedimentation tank (8) and the second sedimentation tank (1) are equipped with several filter inclined plates (4) and several filter outlet tanks (3); A linkage drive component (30) is installed in the scraping push component (2); The first reaction tank (5), the first flocculation tank (9), and the first sedimentation tank (8) have the same structure as the second reaction tank (10), the second flocculation tank (20), and the second sedimentation tank (1), respectively.
2. The wastewater multi-stage rectification adaptive sedimentation treatment device as described in claim 1, characterized in that, The first reaction tank (5) has a connecting groove (51) on its side wall, and the two first reaction tanks (5) are connected through the connecting groove (51). The bottom of the side wall of the first reaction tank (5) has a water passage hole (52), and the first reaction tank (5) is connected to the first flocculation tank (9) through the water passage hole (52).
3. The wastewater multi-stage rectification adaptive sedimentation treatment device as described in claim 1, characterized in that, The first flocculation tank (9) has a through groove (92) on its side wall. The first flocculation tank (9) is connected to the first sedimentation tank (8) through the through groove (92). The first flocculation tank (9) has a round hole (91) at its bottom.
4. The wastewater multi-stage rectification adaptive sedimentation treatment device as described in claim 3, characterized in that, A baffle (81) is installed on the bottom plate of the first sedimentation tank (8). An inclined plate (82) is installed between one end of the baffle (81) and the bottom plate of the first sedimentation tank (8). An annular slope (83) is provided between the other end of the inclined plate (82) and the side plate of the first sedimentation tank (8). A frustum-shaped storage groove (84) is also opened on the bottom plate of the first sedimentation tank (8). The frustum-shaped storage groove (84) is located below the annular slope (83). Several arc-shaped walls (85) are provided on the inclined plate (82) and the side plate wall of the first sedimentation tank (8). The arc-shaped walls (85) are located above the annular slope (83). A guide plate (86) is provided between the two side walls of the first sedimentation tank (8). The guide plate (86) is parallel to the baffle (81).
5. The wastewater multi-stage rectification adaptive sedimentation treatment device as described in claim 1, characterized in that, The hybrid component (6) includes: A placement plate (62) is installed on top of several first reaction tanks (5), and several first rotary motors (61) are installed on the top of the placement plate (62). A drive rod (63) is installed at the bottom output end of the first rotary motor (61). The bottom of the drive rod (63) passes through the placement plate (62). Several rotating disks (64) are installed on the drive rod (63). Several bevel teeth (65) are installed at the bottom of the rotating disk (64).
6. The wastewater multi-stage rectification adaptive sedimentation treatment device as described in claim 1, characterized in that, The flocculation stirring assembly (7) includes: A connecting plate (71) is installed above the first flocculation tank (9) or the second flocculation tank (20); A second rotary motor (72) is installed on the top of the connecting plate (71). A rotary shaft (75) is installed at the bottom output end of the second rotary motor (72), and the bottom of the rotary shaft (75) extends out of the connecting plate (71). Several connecting plates (74) are installed on the side wall of the first flocculation tank (9); An annular guide barrel (73) is installed between several of the connecting plates (74); Several toothed plates (76) are installed on the bottom periphery of the rotating shaft (75).
7. The wastewater multi-stage rectification adaptive sedimentation treatment device as described in claim 4, characterized in that, The scraping push assembly (2) includes: The mounting plate (24) has an internal mounting groove. The mounting plate (24) is installed on the top of the first sedimentation tank (8) or the second sedimentation tank (1). A drive motor (21) is installed on the top of the mounting plate (24). A first gear (22) and a second gear (23) are installed in the mounting groove. The first gear (22) and the second gear (23) mesh. The first gear (22) is installed at the bottom output end of the drive motor (21). A limit sleeve (25) is installed at the bottom of the mounting plate (24). A bushing (211) is installed at the bottom of the frustum-shaped storage groove (84); The rotating shaft (26) is mounted on the top of the second gear (23), and the bottom of the rotating shaft (26) passes through the bottom plate of the mounting plate (24) and the limiting sleeve (25) and is inserted into the bushing (211); Several trapezoidal plates (210) are installed on the bottom periphery of the rotating shaft (26), and the trapezoidal plates (210) are arranged in the frustum-shaped storage groove (84); An annular sleeve (29) is installed on the rotating shaft (26). The annular sleeve (29) is located above the trapezoidal plate (210). Several sleeves (28) are provided on the outer periphery of the annular sleeve (29). An annular scraper (219) is installed at the bottom of the sleeve (28). An I-shaped slide bar (215) is slidably connected in the sleeve (28). A connecting rod (214) is installed at the outer end of the I-shaped slide bar (215). A first scraper (27) is installed at the outer end of the connecting rod (214). The first scraper (27) has arc-shaped surfaces at both ends. A drive rack (217) is symmetrically arranged on the side of the middle part of the I-shaped slide bar (215). A permanent magnet (218) is provided on the inner end surface of the I-shaped slide bar (215). The upper end of the linkage component (216) is connected to the I-shaped slide bar (215), and the bottom of the linkage component (216) is connected to the second scraper (212).
8. The wastewater multi-stage rectification adaptive sedimentation treatment device as described in claim 7, characterized in that, The linkage component (216) includes: T-shaped connecting cylinders (2161) are arranged in pairs. The top of the cylinder is installed on the inner wall of the top of the sleeve (28). The bottom of the T-shaped connecting cylinder (2161) is rotatably connected to a linkage gear (2165). The linkage gear (2165) has an internal thread groove at its center. The linkage gear (2165) meshes with the drive rack (217). The threaded lifting rod (2162) is provided in pairs and screwed into the two internal threaded grooves; The crossbar (2164) is connected at both ends to the bottom of the two threaded lifting rods (2162). A connecting rod (2163) is installed at the bottom of the crossbar (2164). The bottom of the connecting rod (2163) passes through the sleeve (28) and the annular scraper (219) and is equipped with the second scraper (212) at the end.
9. The wastewater multi-stage rectification adaptive sedimentation treatment device as described in claim 7, characterized in that, The upper sidewall of the rotating shaft (26) has several rectangular grooves. The linkage drive component (30) includes: An anisotropic magnet (301) is installed on the inner side of the bottom of the limiting sleeve (25); Several coils (302) are arranged in the rotating shaft (26), a portion of one coil (302) passes through two symmetrical rectangular slots, and an energized coil (304) is installed between the two ends of the coil (302). An electromagnet (303) is installed in the rotating shaft (26), with both ends of the electromagnet (303) extending out of the rotating shaft (26). Both ends of the electromagnet (303) are directly opposite the permanent magnet (218), and the coil (302) is located outside the electromagnet (303).
10. The wastewater multi-stage rectification adaptive sedimentation treatment device as described in claim 1, characterized in that, The bottom sides of the first flocculation tank (9), the first sedimentation tank (8), the second flocculation tank (20), and the second sedimentation tank (1) are provided with T-shaped pipes (40). One end of the T-shaped pipe (40) extends into the first sedimentation tank (8) or the second sedimentation tank (1), and the other end of the T-shaped pipe (40) is located on the outermost side. A section of the T-shaped pipe (40) is also located in the first flocculation tank (9) or the second flocculation tank (20).
