A multi-stage separation flotation cell structure

By using a combination structure of bubble screen plate with return spring and movable plug plate in the flotation cell, the problem of bubble clogging was solved, the bubble distribution was made uniform, and the recovery rate of copper ore and the grade of concentrate were improved.

CN224475131UActive Publication Date: 2026-07-10HAMI DINGXIN COPPER CO LTD
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Patent Information

Application Number
CN202521348574.8
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-06-30
Publication Date
2026-07-10
Estimated Expiration
2035-06-30

AI Technical Summary

Technical Problem

In multi-stage separation flotation cell structures, aerated screen plates are prone to clogging of bubble holes due to copper ore or high-hardness gangue that has not been completely dissociated during the crushing process. This results in uneven bubble distribution, affecting copper recovery rate and concentrate grade.

Method used

The system employs a combination structure of a bubble sieve plate, a return spring, and a movable plug plate. By using a negative pressure fan to circulate air and utilizing the elasticity of the return spring, it automatically seals and unblocks the bubble pores, preventing clogging and ensuring uniform bubble distribution.

Benefits of technology

It effectively prevents bubble clogging, ensures the normal operation of multi-stage separation flotation cells, and improves concentrate grade and overall recovery rate.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the technical field of floatation tank, concretely to a multistage separation type floatation tank structure, include: rough separation floatation tank body, fine separation floatation tank body, sweep separation floatation tank body and floatation flow channel, the floatation flow channel is located rough separation floatation tank body and fine separation floatation tank body and the upper end of sweep separation floatation tank body, bubble sieve plate, the top of bubble sieve plate is provided with a plurality of equidistance distribution's bubble hole, the bottom fixed connection of bubble sieve plate inner chamber has a plurality of equidistance distribution's return spring. The utility model has the ability of bubble sieve plate anti - jamming while guaranteeing multistage separation type floatation ability, guarantees the normal operation of multistage separation type floatation tank structure's floatation work, and helps to improve concentrate grade and comprehensive recovery rate.
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Description

Technical Field

[0001] This utility model relates to the field of flotation cell technology, specifically a multi-stage separation flotation cell structure. Background Technology

[0002] A flotation cell is a container used in flotation equipment to perform the flotation process. The main function of a flotation cell is to separate valuable minerals from waste rock in ores using the froth flotation method. Flotation cells are widely used in mineral processing and beneficiation industries, such as copper, lead-zinc, molybdenum, and gold mines.

[0003] Currently, copper mines are characterized by complexity and diversity. When copper mines contain associated metals such as lead, zinc, and molybdenum, they need to be separated one by one through multi-stage flotation to avoid mixing with useful minerals. This necessitates the use of multi-stage separation flotation cell structures to improve concentrate grade and overall recovery rate. However, in multi-stage separation flotation cell structures, aerated screen plates are prone to clogging of bubble pores due to copper ore that has not been completely liberated during the crushing process, high-hardness gangue, or sludge covering the screen plate surface. This clogged bubble pores of the aerated screen plates result in uneven bubble distribution, forming bubble-free zones, which in turn affects copper recovery rate and leads to a decrease in concentrate grade. Therefore, we propose a multi-stage separation flotation cell structure. Utility Model Content

[0004] The purpose of this invention is to provide a multi-stage separation flotation cell structure that has the advantage of preventing the aerated screen plate from clogging the bubble pores. This solves the problem that in multi-stage separation flotation cell structures, the aerated screen plate is easily clogged by copper ore that has not been completely separated in the crushing process, high-hardness gangue, or sludge covering the surface of the screen plate. The clogged aerated screen plate will cause uneven bubble distribution, forming bubble-free zones, which will affect the copper recovery rate and reduce the concentrate grade.

[0005] To achieve the above objectives, this utility model provides the following technical solution: a multi-stage separation flotation cell structure, comprising:

[0006] The flotation system includes a roughing separation flotation cell, a cleaning separation flotation cell, a scavenging separation flotation cell, and a flotation channel, wherein the flotation channel is located at the upper end of the roughing separation flotation cell, the cleaning separation flotation cell, and the scavenging separation flotation cell;

[0007] A bubble sieve plate, wherein the top of the bubble sieve plate has multiple equally spaced bubble holes, the bottom of the inner cavity of the bubble sieve plate is fixedly connected to multiple equally spaced return springs, the top of the return springs is fixedly connected to a movable plug plate that slides inside the bubble sieve plate, and the top of the movable plug plate is fixedly connected to multiple equally spaced sealing rods.

[0008] A negative pressure blower is fixedly installed at the lower end of one side of the roughing separation flotation cell, the cleaning separation flotation cell, and the scavenging separation flotation cell. The output end of the negative pressure blower is connected to the upper end of one side of the bubble screen plate by a duct, and the lower end of the rear side of the bubble screen plate is connected to a vent pipe extending to the bottom of the negative pressure blower.

[0009] Preferably, a guide pipe is connected to the right side of the flotation channel.

[0010] Preferably, the bubble screen plate is disposed at the bottom of the inner cavity of the roughing separation flotation cell, the cleaning separation flotation cell, and the scavenging separation flotation cell.

[0011] Preferably, the sealing rod is adapted to the bubble hole, and the sealing rod is located inside the bubble hole.

[0012] Preferably, the movable stopper is located at the middle of the inner cavity of the bubble screen plate, and the top of the movable stopper is located below the air guide tube.

[0013] Compared with the prior art, the beneficial effects of this utility model are as follows:

[0014] This invention ensures the multi-stage separation flotation capability while also preventing the bubble screen plate from clogging, thus guaranteeing the normal operation of the multi-stage separation flotation cell structure and helping to improve concentrate grade and overall recovery rate. Attached Figure Description

[0015] Figure 1 This is a first-view structural diagram of the present invention;

[0016] Figure 2 This is a schematic diagram of the cross-sectional structure of the present invention from a second perspective;

[0017] Figure 3 This is a schematic diagram of the unfolded structure of the bubble screen plate and movable stopper plate of this utility model;

[0018] Figure 4 This is a schematic diagram of the cooperative structure of the reset spring and the movable stopper plate of this utility model.

[0019] In the diagram: 1. Roughing separation flotation cell; 2. Cleaning separation flotation cell; 3. Sweeping separation flotation cell; 4. Flotation channel; 401. Guide pipe; 5. Negative pressure fan; 501. Bubble screen plate; 502. Movable plug plate; 503. Sealing rod; 504. Bubble hole; 505. Return spring; 506. Air guide pipe; 507. Vent pipe. Detailed Implementation

[0020] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.

[0021] In the description of this utility model, unless otherwise stated, "a plurality of" means two or more; the terms "upper," "lower," "left," "right," "inner," "outer," "front end," "rear end," "head," "tail," etc., indicate the orientation or positional relationship 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. In addition, the terms "first," "second," "third," etc., are used for descriptive purposes only and should not be construed as indicating or implying relative importance.

[0022] In the description of this utility model, it should be noted that, unless otherwise explicitly specified and limited, the terms "connected" and "linked" 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. Those skilled in the art can understand the specific meaning of the above terms in this utility model based on the specific circumstances.

[0023] The components of this application, including the roughing separation flotation cell 1, the fine separation flotation cell 2, the scavenging separation flotation cell 3, the flotation channel 4, the guide pipe 401, the negative pressure fan 5, the bubble screen plate 501, the movable plug plate 502, the sealing rod 503, the bubble hole 504, the reset spring 505, the air guide pipe 506, and the air vent pipe 507, are all general standard parts or parts known to those skilled in the art. Their structure and principle can be learned by those skilled in the art through technical manuals or conventional experimental methods.

[0024] Example 1

[0025] Please see Figures 1-4 As shown, this utility model provides a technical solution: a multi-stage separation flotation cell structure, comprising:

[0026] The flotation tank consists of a roughing separation flotation cell 1, a cleaning separation flotation cell 2, a scavenging separation flotation cell 3, and a flotation channel 4. The flotation channel 4 is located at the upper end of the roughing separation flotation cell 1, the cleaning separation flotation cell 2, and the scavenging separation flotation cell 3.

[0027] The bubble screen plate 501 has multiple equally spaced bubble holes 504 on its top. Multiple equally spaced return springs 505 are fixedly connected to the bottom of the inner cavity of the bubble screen plate 501. A movable plug plate 502 that slides inside the bubble screen plate 501 is fixedly connected to the top of the return springs 505. Multiple equally spaced sealing rods 503 are fixedly connected to the top of the movable plug plate 502.

[0028] The negative pressure fan 5 is fixedly installed at the lower end of one side of the roughing separation flotation tank 1, the cleaning separation flotation tank 2, and the scavenging separation flotation tank 3. The output end of the negative pressure fan 5 is connected to the upper end of one side of the bubble screen plate 501 by a guide pipe 506.

[0029] The bubble screen plate 501 is located at the bottom of the inner cavity of the roughing separation flotation tank 1, the cleaning separation flotation tank 2, and the scavenging separation flotation tank 3. The plugging rod 503 is adapted to the bubble hole 504 and is located inside the bubble hole 504. The movable plug plate 502 is located at the middle of the inner cavity of the bubble screen plate 501 and the top of the movable plug plate 502 is located below the air guide pipe 506.

[0030] This technical solution, through the arrangement of a roughing separation flotation tank 1, a cleaning separation flotation tank 2, a scavenging separation flotation tank 3, and a flotation channel 4, allows the ore discharged from the roughing separation flotation tank 1 to be fed into the cleaning separation flotation tank 2 via the flotation channel 4. Then, after flotation again in the cleaning separation flotation tank 2, the ore is fed into the scavenging separation flotation tank 3 via the corresponding flotation channel 4. The ore after further scavenging flows to the next stage of the process via the corresponding flotation channel 4, thus enabling multi-stage separation flotation of copper ore. Through the arrangement of the bubble screen plate 501, during flotation operations in the roughing separation flotation tank 1, the cleaning separation flotation tank 2, and the scavenging separation flotation tank 3, the negative pressure fan 5 can introduce gas into the upper end of the inner cavity of the bubble screen plate 501 via the air guide pipe 506. As the negative pressure at the upper end of the inner cavity of the bubble screen plate 501 increases, it forces the movable plug plate 502 to the bubble screen plate 501. The inner cavity moves downwards, and the movement of the movable plug plate 502 compresses the return spring 505. At the same time, the gas at the lower end of the inner cavity of the bubble screen plate 501 can be discharged outwards through the vent pipe 507. When the movable plug plate 502 moves downwards, it will drive the sealing rod 503 to exit the bubble hole 504. Then, as the negative pressure fan 5 continues to input gas, the gas can be discharged outwards through the bubble hole 504, ensuring the normal operation of flotation. After the flotation is completed, the negative pressure fan 5 stops working, and as the negative pressure at the upper end of the inner cavity of the bubble screen plate 501 decreases, the compressed return spring 505 can drive the movable plug plate 502 to reset. The reset movable plug plate 502 will drive the sealing rod 503 to re-insert into the bubble hole 504. At this time, the reset sealing rod 503 will protrude from the top of the bubble screen plate 501, thus preventing the bubble screen plate 501 from becoming blocked and ensuring the normal operation of the bubble screen plate 501.

[0031] It should be noted that the flotation channel 4 on the roughing separation flotation cell 1 is connected to one side of the cleaning separation flotation cell 2, while the flotation channel 4 of the cleaning separation flotation cell 2 is connected to one side of the scavenging separation flotation cell 3, thereby realizing the flow during multi-stage mineral flotation. In addition, the roughing separation flotation cell 1, the cleaning separation flotation cell 2, and the scavenging separation flotation cell 3 are all equipped with real-time water replenishment pipes to ensure the liquid level in the roughing separation flotation cell 1, the cleaning separation flotation cell 2, and the scavenging separation flotation cell 3. The liquid level is monitored in real time by a level gauge, and it is not just the flow between flotation minerals. Since this is a mature and conventional method in the existing technology, it will not be described in detail here.

[0032] Example 2

[0033] Based on Embodiment 1, this utility model is as follows: Figures 1-4 As shown, a guide pipe 401 is connected to the right side of the flotation channel 4.

[0034] This technical solution: By setting up the guide pipe 401, the minerals after multi-stage separation flotation can be diverted and brought into the process.

[0035] It should be noted that the negative pressure fan 5, the roughing separation flotation cell 1, the cleaning separation flotation cell 2, and the scavenging separation flotation cell 3 used in this structure can all be purchased directly from the market. At the same time, the connection methods and electrical connections of each component adopt mature conventional methods in the existing technology, so they will not be described in detail here.

[0036] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of this utility model, and are not intended to limit the scope of protection of this utility model. Although this utility model has been described in detail with reference to preferred embodiments, those skilled in the art should understand that modifications or equivalent substitutions can be made to the technical solutions of this utility model without departing from the essence and scope of the technical solutions of this utility model.

Claims

1. A multi-stage separation flotation cell structure, characterized in that, include: The flotation tank consists of a roughing separation flotation tank (1), a cleaning separation flotation tank (2), a scavenging separation flotation tank (3), and a flotation channel (4), wherein the flotation channel (4) is located at the upper end of the roughing separation flotation tank (1), the cleaning separation flotation tank (2), and the scavenging separation flotation tank (3); A bubble sieve plate (501) has multiple equally spaced bubble holes (504) on its top. Multiple equally spaced return springs (505) are fixedly connected to the bottom of the inner cavity of the bubble sieve plate (501). A movable plug plate (502) that slides inside the bubble sieve plate (501) is fixedly connected to the top of the return springs (505). Multiple equally spaced sealing rods (503) are fixedly connected to the top of the movable plug plate (502). A negative pressure fan (5) is fixedly installed at the lower end of one side of the roughing separation flotation tank (1), the cleaning separation flotation tank (2), and the scavenging separation flotation tank (3). The output end of the negative pressure fan (5) is connected to the upper end of one side of the bubble screen plate (501) by a guide pipe (506). The lower end of the rear side of the bubble screen plate (501) is connected to a ventilation pipe (507) extending to the lower part of the negative pressure fan (5).

2. The multi-stage separation flotation cell structure according to claim 1, characterized in that: The right side of the flotation channel (4) is connected to a guide pipe (401).

3. The multi-stage separation flotation cell structure according to claim 1, characterized in that: The bubble screen plate (501) is disposed at the bottom of the inner cavity of the roughing separation flotation tank (1), the fine separation flotation tank (2), and the scavenging separation flotation tank (3).

4. The multi-stage separation flotation cell structure according to claim 1, characterized in that: The plugging rod (503) is adapted to the bubble hole (504), and the plugging rod (503) is located inside the bubble hole (504).

5. The multi-stage separation flotation cell structure according to claim 1, characterized in that: The movable stopper plate (502) is located at the middle of the inner cavity of the bubble screen plate (501), and the top of the movable stopper plate (502) is located below the air guide pipe (506).