Micro-flocculation fiber rotary disc filtering device
By combining the flocculation baffles and filter plates of the micro-flocculation fiber disc filter device, the problem of high energy consumption in air flotation sedimentation tanks is solved, achieving a low-energy and high-efficiency sewage purification effect.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- YUHUAN JINGHUA GROUP
- Filing Date
- 2025-05-07
- Publication Date
- 2026-04-17
AI Technical Summary
Existing air flotation sedimentation tanks consume a lot of energy when purifying wastewater and are difficult to remove suspended solids and algae efficiently.
The micro-flocculation fiber disc filter device uses flocculation baffles and filter plates to remove suspended particles and algae in a flowing state, achieving purification through flocculation and adsorption, avoiding the need for aeration.
It achieves low-energy wastewater purification, effectively removes suspended particles and algae, and reduces treatment costs.
Smart Images

Figure CN224132813U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of water treatment equipment, and in particular to a micro-flocculation fiber disc filter device. Background Technology
[0002] Currently, a large amount of wastewater (containing a large amount of suspended solids) is generated in industrial and agricultural production. Wastewater needs to be purified before discharge. In order to adsorb and treat the suspended solids in wastewater, patent publication document CN213977272U discloses an air flotation sedimentation tank that can treat wastewater. The air flotation sedimentation tank shown in this structure uses air flotation to purify and remove pollutants from wastewater. Because this air flotation sedimentation tank needs to continuously pump high-pressure gas into the water body during purification, the energy consumption of this air flotation sedimentation tank is very high when treating water. Utility Model Content
[0003] To address the aforementioned problems, this invention proposes a micro-flocculation fiber rotary filter device. By using flocculation baffles and filter plates, it removes suspended particles and algae from wastewater while it is in a flowing state, thus purifying the wastewater. Furthermore, no aeration is required during the wastewater treatment process, resulting in relatively low energy consumption throughout the entire process.
[0004] The technical solution adopted by this utility model is as follows:
[0005] A micro-flocculation fiber rotary filter device includes a tank body, in which a first processing chamber, a second processing chamber, and a third processing chamber are disposed. The second processing chamber is in communication with the first and third processing chambers. The device also includes a plurality of flocculation baffles and a plurality of filter plates. The flocculation baffles are disposed in the second processing chamber, and adjacent flocculation baffles are not in contact with each other. The filter plates are disposed in the third processing chamber, and adjacent filter plates are parallel and not in contact with each other.
[0006] The working process of this micro-flocculation fiber rotary filter device is as follows: first, the sewage enters the first treatment chamber, then the second treatment chamber, and finally the third treatment chamber.
[0007] The wastewater treatment process of this micro-flocculation fiber rotary filter device is as follows: First, PAC (aluminum chloride treatment agent) is added to the wastewater when it enters the first treatment chamber. Then, PAM (polyacrylamide) is added. At this point, suspended particles in the wastewater begin to flocculate. The flocculated wastewater then flows to the second treatment chamber, where it comes into contact with flocculation baffles. Suspended particles adhere to these baffles, providing initial purification. After purification, the wastewater flows further to the filter plates. Algae and other particles in the wastewater are further adsorbed by the filter plates and eventually leave the tank.
[0008] Therefore, in this micro-flocculation fiber rotary filter device, by using flocculation baffles and filter plates, suspended particles and algae are removed from the wastewater in a flowing state, thus purifying the wastewater. Moreover, no aeration is required during the wastewater treatment process, and the energy consumption of the entire process is relatively low.
[0009] Specifically, in this device, the filter is a fiber disc filter.
[0010] Optionally, the flocculation baffle is a zigzag-shaped flocculation baffle, and the flocculation baffle is disposed on the top or bottom of the tank.
[0011] The purpose of using zigzag-shaped flocculation baffles is to allow suspended particles in the wastewater to adhere to the flocculation baffles as much as possible.
[0012] Optionally, it also includes a stirring paddle, which is rotatably disposed inside the first processing chamber, and a drive motor is disposed outside the tank body, the drive motor cooperating with the stirring paddle.
[0013] Specifically, the drive motor drives the agitator to rotate, and the rotation of the agitator enables the suspended particles in the first processing chamber to fully react with the reagent, and then fully flocculate after the reaction.
[0014] Optionally, it also includes an inlet pipe and an outlet pipe, both of which are installed on the tank body. The inlet pipe is connected to the first processing chamber, and the outlet pipe is connected to the third processing chamber.
[0015] Wastewater enters the first treatment chamber through the inlet pipe, and after treatment, it enters the outlet pipe through the third treatment chamber.
[0016] Optionally, the tank body is connected to a sludge discharge pipe, which is connected to the second processing chamber.
[0017] The purpose of the sludge discharge pipe is to discharge sludge. After suspended particles adhere to the flocculation baffles, they will eventually fall to the bottom of the tank and settle as sludge.
[0018] Optionally, a cleaning pipe is provided inside the third processing chamber, and a suction pump is connected to the cleaning pipe. The suction pump is located outside the tank.
[0019] The inlet of the cleaning tube is located on one side of the filter. The suction pump is connected to the cleaning tube. When the suction pump is turned on, it can remove the dirt attached to the filter, thereby cleaning and regenerating the filter.
[0020] Optionally, the filter is a disc-shaped filter.
[0021] Optionally, the first processing cavity and the third processing cavity are located on both sides of the second processing cavity.
[0022] The beneficial effects of this utility model are: by using flocculation baffles and filter sheets, suspended particles and algae are removed from the sewage in a flowing state, thus purifying the sewage. Moreover, no aeration is required during the sewage treatment process, and the energy consumption of the entire process is relatively low. Attached Figure Description
[0023] To more clearly illustrate the technical solutions in the embodiments of this application or the prior art, the drawings used in the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments recorded in this utility model. For those skilled in the art, other drawings can be obtained based on these drawings.
[0024] Figure 1 This is a schematic diagram of the water flow direction when the micro-flocculation fiber disc filter is working;
[0025] Figure 2 This is a simplified schematic diagram of a micro-flocculation fiber rotary filter device.
[0026] The figures are labeled as follows: 1. Inlet pipe; 2. Drive motor; 3. Tank body; 301. First processing chamber; 302. Second processing chamber; 303. Third processing chamber; 4. Stirring blade; 5. Sludge discharge pipe; 6. Flocculation baffle; 7. Filter plate; 8. Outlet pipe; 9. Cleaning pipe; 10. Suction pump. Detailed Implementation
[0027] To make the above-mentioned objectives, features and advantages of this utility model more apparent and understandable, the specific embodiments of this utility model will be described in detail below with reference to the accompanying drawings.
[0028] Many specific details are set forth in the following description in order to provide a full understanding of the present invention. However, the present invention may also be implemented in other ways different from those described herein. Those skilled in the art can make similar extensions without departing from the spirit of the present invention. Therefore, the present invention is not limited to the specific embodiments disclosed below.
[0029] In the description of this application, it should be noted that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to limit the exemplary embodiments according to this application. For ease of description, the dimensions of the various parts shown in the drawings are not drawn to actual scale. Techniques, methods, and devices known to those skilled in the art may not be discussed in detail, but where appropriate, such techniques, methods, and devices should be considered part of the specification. In all examples shown and discussed herein, any specific values should be interpreted as merely exemplary and not as limitations. Therefore, other examples of exemplary embodiments may have different values. It should be noted that similar reference numerals and letters in the following drawings denote similar items; therefore, once an item is defined in one drawing, it need not be further discussed in subsequent drawings.
[0030] As attached Figure 1 and appendix Figure 2 As shown, a micro-flocculation fiber rotary filter device includes a tank 3, which contains a first processing chamber 301, a second processing chamber 302, and a third processing chamber 303. The second processing chamber 302 is in communication with the first processing chamber 301 and the third processing chamber 303. The device also includes several flocculation baffles 6 and several filter sheets 7. The flocculation baffles 6 are disposed in the second processing chamber 302, and adjacent flocculation baffles 6 are not in contact with each other. The filter sheets 7 are disposed in the third processing chamber 303, and adjacent filter sheets 7 are parallel and not in contact with each other.
[0031] The working process of this micro-flocculation fiber rotary filter device is as follows: first, the sewage enters the first treatment chamber 301, then the second treatment chamber 302, and finally the third treatment chamber 303.
[0032] The wastewater treatment process of this micro-flocculation fiber rotary filter device is as follows: First, PAC (aluminum chloride treatment agent) is added to the wastewater when it enters the first treatment chamber 301. Then, PAM (polyacrylamide) is added. At this point, suspended particles in the wastewater begin to flocculate. The flocculated wastewater then flows to the second treatment chamber 302, where it comes into contact with the flocculation baffles 6. Particles suspended in the water adhere to the flocculation baffles 6, thus providing initial purification. After purification by the flocculation baffles 6, the wastewater flows further to the filter plates 7. Algae and other particles in the wastewater are further adsorbed by the filter plates 7 after passing through them, and finally leave the tank 3.
[0033] Therefore, in this micro-flocculation fiber rotary filter device, by using the flocculation baffle 6 and filter plate 7, suspended particles and algae are removed from the wastewater in a flowing state, which purifies the wastewater. Moreover, no aeration is required during the wastewater treatment process, and the energy consumption is relatively low throughout the entire process.
[0034] Specifically, in this device, filter 7 is a fiber filter 7.
[0035] As attached Figure 1 and appendix Figure 2 As shown, the flocculation baffle 6 is a zigzag-shaped flocculation baffle 6, and the flocculation baffle 6 is set on the top or bottom of the tank body 3.
[0036] The zigzag-shaped flocculation baffle 6 is used to allow suspended particles in the wastewater to adhere to the flocculation baffle 6 as much as possible.
[0037] As attached Figure 1 and appendix Figure 2 As shown, it also includes a stirring paddle, which is rotatably disposed in the first processing chamber 301. A drive motor 2 is disposed outside the tank body 3, and the drive motor 2 is engaged with the stirring paddle.
[0038] Specifically, the drive motor 2 drives the stirring paddle to rotate. The rotation of the stirring paddle causes the suspended particles in the first processing chamber 301 to react fully with the agent, and then fully flocculate after the reaction.
[0039] As attached Figure 1 and appendix Figure 2 As shown, it also includes an inlet pipe 1 and an outlet pipe 8. Both the inlet pipe 1 and the outlet pipe 8 are installed on the tank body 3. The inlet pipe 1 is connected to the first processing chamber 301, and the outlet pipe 8 is connected to the third processing chamber 303.
[0040] Wastewater enters the first treatment chamber 301 from the inlet pipe 1, and after treatment, it enters the outlet pipe 8 from the third treatment chamber 303.
[0041] As attached Figure 1 and appendix Figure 2 As shown, a sludge discharge pipe 5 is connected to the tank body 3, and the sludge discharge pipe 5 is connected to the second processing chamber 302.
[0042] The function of the sludge discharge pipe 5 is to discharge sludge. After the suspended particles adhere to the flocculation baffle 6, they will eventually fall to the bottom of the tank and adhere as sediment.
[0043] As attached Figure 1 and appendix Figure 2 As shown, a cleaning pipe 9 is installed in the third processing chamber 303, and a suction pump 10 is connected to the cleaning pipe 9. The suction pump 10 is located outside the tank body 3.
[0044] The inlet of the cleaning pipe 9 is located on one side of the filter 7. The suction pump 10 is connected to the cleaning pipe 9. When the suction pump is turned on, it can remove the dirt attached to the filter 7, thereby cleaning and regenerating the filter 7.
[0045] As attached Figure 1 and appendix Figure 2 As shown, filter 7 is a disc-shaped filter 7.
[0046] As attached Figure 1 and appendix Figure 2 As shown, the first processing cavity 301 and the third processing cavity 303 are located on both sides of the second processing cavity 302.
[0047] The above-described embodiments only illustrate some aspects of the present invention, and while the descriptions are specific and detailed, they should not be construed as limiting the scope of the present invention. It should be noted that those skilled in the art can still modify the technical solutions described in the foregoing embodiments or make equivalent substitutions for some of the technical features. Any modifications, equivalent substitutions, or improvements made within the spirit and principles of this utility model should be included within the protection scope of this utility model.
Claims
1. A micro-flocculation fiber rotary disc filter device, comprising a tank, wherein a first processing chamber, a second processing chamber, and a third processing chamber are disposed within the tank, the second processing chamber being in communication with the first and third processing chambers, characterized in that, It also includes several flocculation baffles and several filter sheets. The flocculation baffles are disposed in the second processing chamber and adjacent flocculation baffles are not in contact with each other. The filter sheets are disposed in the third processing chamber and adjacent filter sheets are parallel and not in contact with each other.
2. A micro-flocculator fiber rotating disc filter apparatus according to claim 1, wherein, The flocculation baffle is a zigzag-shaped flocculation baffle, and the flocculation baffle is set on the top or bottom of the tank.
3. A micro-flocculator fiber rotating disc filter apparatus according to claim 1, wherein, It also includes a stirring paddle, which is rotatably disposed inside the first processing chamber, and a drive motor is disposed outside the tank body, which works together with the stirring paddle.
4. A micro-flocculator fiber rotating disc filter apparatus according to claim 1, wherein, It also includes an inlet pipe and an outlet pipe, both of which are installed on the tank body. The inlet pipe is connected to the first processing chamber, and the outlet pipe is connected to the third processing chamber.
5. A micro-flocculator fiber rotating disc filter apparatus according to claim 1 wherein, The tank is equipped with a sludge discharge pipe, which is connected to the second processing chamber.
6. The micro-flocculation fiber rotary filter device according to claim 1, characterized in that, The third processing chamber is equipped with a cleaning pipe, and a suction pump is connected to the cleaning pipe. The suction pump is located outside the tank.
7. A micro-flocculator fiber rotating disc filter apparatus according to claim 1 wherein, The filter is a disc-shaped filter.
8. A micro-flocculator fiber rotating disc filter apparatus as claimed in claim 1 wherein, The first processing cavity and the third processing cavity are located on both sides of the second processing cavity.
Citation Information
Patent Citations
Efficient air flotation sedimentation tank
CN213977272U