A novel high-efficiency integrated filtration device for water treatment

By introducing baffle plate + guide tube stirring and fiber ball filtration into the water treatment device, combined with backwashing and air washing technologies, the problems of long flocculation time and easy caking of quartz sand in the existing technology are solved, achieving efficient flocculation and easy-to-clean filtration effect.

CN224942454UActive Publication Date: 2026-11-06SHANDONG SIHAI WATER TREATMENT EQUIP CO LTD
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Patent Information

Application Number
CN202522683302.X
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-12-18
Publication Date
2026-11-06
Estimated Expiration
2035-12-18

AI Technical Summary

Technical Problem

In existing integrated water treatment processes, folded plate flocculation has a long time and poor effect, while quartz sand filtration has high resistance, low flow rate and is prone to caking.

Method used

The process employs a baffle plate and guide tube stirring process in the flocculation zone, combined with filtration in the fiber ball filling zone, and uses backwashing and air washing technologies for cleaning.

Benefits of technology

Shorten flocculation time, improve flocculation efficiency, and achieve a filtration effect that is non-caking and easy to clean.

✦ Generated by Eureka AI based on patent content.

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Abstract

This utility model relates to the field of water treatment technology and provides a novel, highly efficient integrated filtration device for water treatment, comprising: a flocculation zone, a sedimentation zone, and a filtration zone. The flocculation zone and the sedimentation zone are connected, and the filtration zone is located outside the flocculation zone. The flocculation zone includes a flocculation tank, a flocculation baffle zone, a flocculation guide tube, and a flocculation inlet. The sedimentation zone includes an inclined plate filling zone, a water collection tank, a sedimentation product outlet, several sets of sludge storage hoppers, and several sets of sludge discharge pipes. The filtration zone includes an inlet tank, an inlet water distribution tank, a water storage zone, and a filtration product outlet. Therefore, this utility model employs a baffle plate + guide tube stirring process in the flocculation zone, which can shorten the flocculation time and improve the flocculation efficiency. The filtration zone uses fiber filter media, achieving a non-caking and easy-to-clean effect.
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Description

Technical Field

[0001] This utility model relates to the field of water treatment technology, and in particular to a novel high-efficiency integrated filtration device for water treatment. Background Technology

[0002] Existing technical solutions mainly employ integrated water treatment processes through folded plate flocculation, inclined plate sedimentation, and quartz sand filtration.

[0003] However, the existing integrated water treatment process has the following drawbacks: 1. Long flocculation time and poor effect of folded plate flocculation; 2. High resistance, low flow rate and easy caking of quartz sand filtration.

[0004] In conclusion, the existing technology obviously has inconveniences and defects in practical use, so it is necessary to improve it. Utility Model Content

[0005] To address the aforementioned shortcomings, this invention provides a novel, highly efficient, integrated water treatment filtration device.

[0006] To achieve the above objectives, this utility model provides a novel high-efficiency integrated filtration device for water treatment, comprising: a flocculation zone, a sedimentation zone, and a filtration zone. The flocculation zone and the sedimentation zone are connected, and the filtration zone is located outside the flocculation zone. The flocculation zone includes a flocculation tank, a flocculation baffle zone, a flocculation guide tube, and a flocculation inlet. The bottom of the flocculation baffle zone is provided with a connecting pipe connected to the flocculation guide tube. The sedimentation zone includes an inclined plate filling zone, a water collection tank, a sedimentation outlet, several sets of sludge storage hoppers, and several sets of sludge discharge pipes. The water collection tank is located at the top of the inclined plate filling zone and is connected to the sedimentation outlet. The several sets of sludge storage hoppers and sludge discharge pipes are all located at the bottom of the inclined plate filling zone. The filtration zone includes an inlet tank, an inlet water distribution tank, a water storage zone, and a filtration outlet. The top of the inlet tank is located below the sedimentation outlet, and the inlet water distribution tank is connected to the inlet tank. The water storage zone is located inside the filtration zone and below it, and is connected to the filtration outlet.

[0007] According to the present invention, a novel high-efficiency integrated water treatment filtration device is provided in the filtration zone, a fiber ball filling zone is provided at the top of the fiber ball filling zone, a fiber ball filter tank is provided at the bottom of the fiber ball filling zone, and a filter plate is provided at the top of the water storage zone.

[0008] According to the present invention, a novel high-efficiency integrated water treatment filtration device is provided on one side of the filtration zone, a backwash water tank is provided on the top of the backwash water tank, and a backwash water inlet is provided on one side of the backwash water tank.

[0009] According to the present invention, a novel high-efficiency integrated water treatment filtration device is provided with an interception frame at the top of the fiber ball filling area.

[0010] According to the present invention, a novel high-efficiency integrated water treatment filtration device is provided at the bottom of one side of the filtration zone, and the air washing inlet is located at the top of the backwash inlet.

[0011] Compared with the prior art, the beneficial effects of this utility model are: The flocculation zone uses a baffle plate + guide tube stirring process, which can shorten the flocculation time and improve the flocculation efficiency; the filtration zone uses fiber filter media to achieve the effect of not caking and easy cleaning. Attached Figure Description

[0012] Figure 1 This is a three-dimensional structural diagram of the present invention from one angle; Figure 2 This is a three-dimensional structural schematic diagram of the present invention from another angle; Figure 3 This is a three-dimensional structural schematic diagram of the present invention from another angle; Figure 4 This is a three-dimensional structural schematic diagram of the present invention from another angle; Figure 5 This is a schematic diagram of the main view structure of this utility model; Figure 6 This is a top view structural schematic diagram of this utility model; In the diagram, 1-flocculation zone, 2-sedimentation zone, 3-flocculation baffle zone, 4-flocculation guide tube, 5-flocculation inlet, 6-sedimentation outlet, 7-filtration zone, 8-fiber ball filling zone, 9-inlet tank, 10-inlet water distribution tank, 11-filtration outlet, 12-backwash inlet, 13-backwash outlet, 14-air washing inlet, 15-connecting pipe, 16-collecting tank, 17-sloping plate filling zone, 18-sludge hopper, 19-sludge discharge pipe, 20-interception frame, 21-filter plate, 22-backwash tank. Detailed Implementation

[0013] To make the objectives, technical solutions, and advantages of this utility model clearer, the present utility model will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely for explaining the present utility model and are not intended to limit the present utility model.

[0014] It should be noted that in the description of this utility model, the terms "upper", "lower", "left", "right", "inner", "outer", etc., indicating the direction or positional relationship are based on the direction or positional relationship shown in the drawings. This is only for the convenience of description and does not indicate or imply that the device or element must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, it should not be construed as a limitation of this utility model.

[0015] Furthermore, it should be noted that, in the description of this utility model, 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 according to the specific circumstances.

[0016] See Figures 1-6 This utility model provides a novel high-efficiency integrated filtration device for water treatment, comprising: a flocculation zone 1, a sedimentation zone 2, and a filtration zone 7. The flocculation zone 1 and the sedimentation zone 2 are connected, and the filtration zone 7 is located outside the flocculation zone 1. The flocculation zone 1 includes a flocculation tank, a flocculation baffle zone 3, a flocculation guide tube 4, and a flocculation inlet 5. The bottom of the flocculation baffle zone 3 is provided with a connecting pipe 15 connected to the flocculation guide tube 4. The sedimentation zone 2 includes an inclined plate filling zone 17, a water collection tank 16, a sedimentation product outlet 6, several sets of sludge storage hoppers 18, and several sets of sludge discharge pipes. 19. The water collection tank 16 is located at the top of the inclined plate filling area 17. The water collection tank 16 is connected to the sedimentation water outlet 6. Several sets of sludge storage hoppers 18 and sludge discharge pipes 19 are located at the bottom of the inclined plate filling area 17. The filtration area 7 includes an inlet tank 9, an inlet water distribution tank 10, a water storage area, and a filter water outlet 11. The top of the inlet tank 9 is located below the sedimentation water outlet 6. The inlet water distribution tank 10 is connected to the inlet tank 9. The water storage area is located inside the filtration area 7 and is connected to the filter water outlet 11.

[0017] See Figures 1-6 Preferably, the filtration zone 7 of this invention is provided with a fiber ball filling zone 8, the top of the fiber ball filling zone 8 is provided with a fiber ball filter pool, the bottom of the fiber ball filling zone 8 is provided with a filter plate 21, the filter plate 21 is located at the top of the water storage zone, and the colloidal clumps are filtered and retained through the fiber ball filling zone 8.

[0018] See Figures 1-6Furthermore, the filter area 7 of this utility model is provided with a backwash water tank 22 on one side, a backwash water inlet 12 on the top of the backwash water tank 22, and a backwash drain outlet 13 on one side of the backwash water tank 22. Backwashing can rinse away impurities in the water flow, which is convenient for subsequent use.

[0019] See Figures 1-6 Even better, the top of the fiber ball filling area 8 of this utility model is provided with an interception frame 20, which intercepts the fiber balls.

[0020] See Figures 1-6 Finally, the bottom of one side of the filter zone 7 of this utility model is provided with an air washing inlet 14, which is located at the top of the backwash water inlet 12, and gas is introduced to enhance the friction cleaning of the fiber balls.

[0021] The working principle of this utility model: After adding flocculant to the raw water, it enters the flocculation baffle zone 3 through the flocculation inlet 5. The up-and-down folding of the water flow increases the disturbance of the water flow, promoting the collision of smaller colloids in the water and forming small flocculent clumps. Then, it enters the flocculation guide tube 4 from the bottom through the connecting pipe 15 and flows from bottom to top. Relying on gravity, the flocculent clumps gradually gather, increasing the collision probability and forming larger colloid clumps. A frame structure is provided at the top of the flocculation guide tube 4, and a speed reducer can be installed at the top of the flocculation guide tube 4 to further promote the collision of colloids and form larger flocculent clumps that flow into the sedimentation zone 2.

[0022] Water in flocculation zone 1 flows from top to bottom through the top of flocculation guide tube 4, and then enters sedimentation zone 2 through the bottom of the plate between flocculation zone 1 and sedimentation zone 2. After entering sedimentation zone 2, the water first passes through inclined plate filling area 17. The staff will pre-install honeycomb inclined plates in inclined plate filling area 17. Under the obstruction of the honeycomb inclined plates and the action of its own gravity, the large flocs of water roll down into the sludge storage hopper 18 at the bottom of sedimentation zone 2 and are discharged through sludge discharge pipe 19. Since the water flows from bottom to top in sedimentation zone 2, the water will flow through water collection tank 16 and be collected and flow out from sedimentation water outlet 6.

[0023] Water overflowing from sedimentation outlet 6 enters inlet tank 9. After flowing to inlet distribution tank 10, the water in inlet tank 9 is evenly dispersed and flows into fiber ball filling area 8 to filter and retain colloidal aggregates. The interception frame 20 can intercept the fiber balls. At the same time, the bottom of fiber ball filling area 8 is provided with filter plate 21, which is full of holes and equipped with water caps. Then the water flows to the water storage area and finally flows from the filter tank outlet to the water production tank under static pressure.

[0024] When backwashing is required, the water flows through the backwash inlet 12 to the filter plate 21, and then through the water cap on the filter plate 21 into the fiber ball filtration zone 7. The reverse water flow causes the fiber balls to rise and tumble, thereby rubbing and washing away the attached filter impurities. The backwash water flows upward to the backwash water tank 22 to carry away the filter impurities and is discharged from the backwash drain 13.

[0025] When air washing is required, the air intake path for air washing is the same as that for backwashing. The principle of air washing is to introduce gas to enhance the friction and cleaning of the fiber balls when they are lifted up during backwashing.

[0026] Of course, there may be other embodiments of this utility model. Without departing from the spirit and essence of this utility model, those skilled in the art can make various corresponding changes and modifications based on this utility model, but these corresponding changes and modifications should all fall within the protection scope of the appended claims of this utility model.

Claims

1. A novel, high-efficiency integrated water treatment filtration device, characterized in that, include: The flocculation zone (1), the sedimentation zone (2) and the filtration zone (7) are connected, and the filtration zone (7) is located outside the flocculation zone (1). The flocculation zone (1) includes a flocculation tank, a flocculation baffle zone (3), a flocculation guide tube (4) and a flocculation inlet (5). The bottom of the flocculation baffle zone (3) is provided with a connecting pipe (15) connected to the flocculation guide tube (4). The sedimentation zone (2) includes an inclined plate filling zone (17), a water collection tank (16), a sedimentation water outlet (6), several sets of sludge storage hoppers (18) and several sets of sludge discharge pipes (19). The water collection tank (16) is located at the top of the inclined plate filling zone (17) and is connected to the sedimentation water outlet (6). The several sets of sludge storage hoppers (18) and the sludge discharge pipes (19) are all located at the bottom of the inclined plate filling zone (17). The filtration zone (7) includes an inlet tank (9), an inlet water distribution tank (10), a water storage area, and a filter water outlet (11). The top of the inlet tank (9) is located below the sedimentation water outlet (6). The inlet water distribution tank (10) is connected to the inlet tank (9). The water storage area is located inside the filtration zone (7) and is connected to the filter water outlet (11).

2. The novel high-efficiency integrated water treatment filtration device according to claim 1, characterized in that, The filtration zone (7) is provided with a fiber ball filling zone (8), the top of the fiber ball filling zone (8) is provided with a fiber ball filter pool, the bottom of the fiber ball filling zone (8) is provided with a filter plate (21), and the filter plate (21) is located at the top of the water storage zone.

3. The novel high-efficiency integrated water treatment filtration device according to claim 1, characterized in that, A backwash water tank (22) is provided on one side of the filtration zone (7), a backwash water inlet (12) is provided on the top of the backwash water tank (22), and a backwash water outlet (13) is provided on one side of the backwash water tank (22).

4. The novel high-efficiency integrated water treatment filtration device according to claim 2, characterized in that, The top of the fiber ball filling area (8) is provided with an intercepting frame (20).

5. The novel high-efficiency integrated water treatment filtration device according to claim 3, characterized in that, The bottom of one side of the filter zone (7) is provided with an air washing inlet (14), which is located at the top of the backwash water inlet (12).