Electroplating liquid impurity removing and filtering device

Abstract

The utility model discloses an electroplating liquid impurity removing and filtering device, and relates to the technical field of electroplating liquid impurity removing. The impurity removal device comprises a water pump, a rough filtration component and an impurity removal component, the impurity removal component comprises an impurity removal liquid annular pipe, an annular pipe sleeve and a mixing assembly, the impurity removal liquid annular pipe is sleeved with the annular pipe sleeve, a set of liquid outlet holes are formed in the annular wall of the inner side of the impurity removal liquid annular pipe in a circumferential array penetrating mode, and the mixing assembly is arranged at a liquid outlet in the lower end of the annular pipe sleeve. The rough filtration part is arranged at the upper end of the annular pipe sleeve; the lower outlet end of the water pump is communicated with the upper end of the rough filtration part. Electroplating liquid is pumped into the rough filtration component through the water pump, so that solid particle impurities in the electroplating liquid are filtered and removed; electroplating liquid with solid particle impurities filtered out flows into the impurity removal component, the impurity removal agent is added into the electroplating liquid through the impurity removal liquid annular pipe in the impurity removal component, the electroplating liquid with the impurity removal agent added is discharged into the electroplating pool again and powered on, and therefore metal ion impurities in the electroplating liquid are removed.

Description

Technical Field

[0001] This utility model belongs to the field of electroplating solution impurity removal technology, and in particular relates to a filtration device for removing impurities from electroplating solutions. Background Technology

[0002] After prolonged production, electroplating solutions accumulate a large number of impurities, including large particles and debris, as well as other metal ions. These metal ion impurities, such as copper, iron, and zinc, can affect the electroplating effect. The deposition potential of these metal ions may differ from that of the target metal, leading to co-deposition and affecting the appearance and performance of the coating. Frequent treatment of the electroplating solution is time-consuming, costly, and can also disrupt the progress of the electroplating process on the production line.

[0003] To address these issues, we provide a filtration device for removing impurities from electroplating solutions. Utility Model Content

[0004] The purpose of this invention is to provide a filtration device for removing impurities from electroplating solutions. A coarse filter is installed at the outlet of a water pump, and a purification component is installed at the outlet of the coarse filter. The water pump pumps the electroplating solution into the coarse filter to remove solid particulate impurities. The electroplating solution after filtration flows into the purification component, where a purification agent is added through a purification liquid loop. The electroplating solution after the addition of the purification agent is discharged back into the electroplating tank and energized, thereby removing metal ion impurities from the electroplating solution.

[0005] To solve the above-mentioned technical problems, this utility model is achieved through the following technical solution:

[0006] This utility model relates to a filtration device for removing impurities from electroplating solutions, comprising a water pump, a coarse filter component, and an impurity removal component. The impurity removal component includes an impurity removal liquid ring pipe, a ring pipe sleeve, and a mixing assembly. The impurity removal liquid ring pipe is fitted inside the ring pipe sleeve. An inlet pipe is connected to the outer wall of the impurity removal liquid ring pipe, and the inlet pipe penetrates the ring pipe sleeve. A set of outlet holes are circumferentially arrayed through the inner wall of the impurity removal liquid ring pipe. The mixing assembly is located at the outlet at the lower end of the ring pipe sleeve. The coarse filter component is located at the upper end of the ring pipe sleeve. The lower outlet end of the water pump is connected to the upper end of the coarse filter component.

[0007] A further feature of this invention is that the coarse filter component includes a coarse filter basket and a basket sleeve. The lower end of the basket sleeve is connected to the annular sleeve, and the upper end of the basket sleeve is connected to the lower outlet end of the water pump through a flange. The coarse filter basket is a tube structure with an open upper end and a closed lower end. A set of coarse filter basket holes are provided through the side wall and bottom of the coarse filter basket. A threaded sleeve is fixed on the upper outer wall of the coarse filter basket, and the threaded sleeve is screwed into the upper inner wall of the basket sleeve.

[0008] A further feature of this invention is that the hybrid assembly includes a convergence sleeve, a rotating propeller, and a rotating shaft seat. The convergence sleeve is fitted onto the lower end of the annular sleeve, and the rotating shaft seat is threaded onto the inner wall of the lower end of the convergence sleeve. A set of connecting arms is circumferentially arrayed on the inner wall of each rotating shaft seat. A rotating shaft sleeve is fixed at the end of the connecting arm set away from the rotating shaft seat. A rotating shaft is fixed at the lower end of the rotating propeller, and the rotating shaft is rotatably installed inside the rotating shaft sleeve.

[0009] A further feature of this invention is that a stirring paddle sleeve is threaded onto the outer side of one end of the rotating shaft that passes through the rotating shaft sleeve, and a set of stirring paddles are fixedly arranged in a circumferential array on the outer sidewall of the stirring paddle sleeve.

[0010] A further feature of this invention is that the converging sleeve is integrally formed from top to bottom by an inlet section, a converging section, and an outlet section, with the converging section gradually converging downwards, and the rotating shaft seat threadedly engaged with the inner wall of the outlet section.

[0011] A further feature of this invention is that a liquid outlet pipe is threaded onto the outer wall of the outlet section, and the stirring paddle is sleeved on the inner wall of the liquid outlet pipe.

[0012] A further feature of this invention is that a flow-regulating sleeve is fixedly sleeved on the inner wall of the outlet pipe. The flow-regulating sleeve is a tubular structure with openings at both the top and bottom. Flow-regulating plates are fixedly arranged in a circumferential array on the inner wall of the flow-regulating sleeve, and the surface of the flow-regulating plates is perpendicular to the pipe axis of the flow-regulating sleeve.

[0013] This utility model has the following beneficial effects:

[0014] 1. This utility model provides a coarse filter component at the outlet of a water pump and a dirt removal component at the outlet of the coarse filter component. The water pump pumps the electroplating solution into the coarse filter component to filter and remove solid particulate impurities in the electroplating solution.

[0015] 2. This utility model removes metal ion impurities from the electroplating solution by allowing the filtered solid particulate impurities to flow into a purification component. A purification agent is then added to the electroplating solution through a purification solution loop pipe in the purification component. After the purification agent is added, the electroplating solution is discharged back into the electroplating tank and electrified, thereby removing the metal ion impurities from the electroplating solution. Attached Figure Description

[0016] To more clearly illustrate the technical solutions of the embodiments of this utility model, the accompanying drawings used in the description of the embodiments will be briefly introduced below.

[0017] Figure 1 This is a schematic diagram of a filter device for removing impurities from an electroplating solution.

[0018] Figure 2 This is an exploded view of the impurity removal liquid loop and the loop sleeve.

[0019] Figure 3 This is an exploded view of the water pump and coarse filter components.

[0020] Figure 4 This is an exploded view of the hybrid components.

[0021] Figure 5 This is an exploded view of the outlet pipe and the flow control sleeve.

[0022] The attached diagram lists the components represented by each number as follows:

[0023] 1-Water pump, 2-Coarse filter component, 201-Coarse filter basket, 201a-Coarse filter basket hole, 201b-Threaded sleeve, 202-Basket sleeve, 3-Impurity removal component, 301-Impurity removal liquid ring pipe, 301a-Inlet pipe, 301b-Outlet hole, 302-Ring pipe sleeve, 303-Mixing assembly, 303a-Converging sleeve, 303a-1-Inlet section, 303a-2-Converging section, 303a-3-Outlet section, 303b-Rotating paddle, 303b-1-Rotating shaft, 303b-2-Agitator shaft sleeve, 303b-3-Agitator, 303c-Rotating shaft seat, 303c-1-Connecting arm, 303c-2-Rotating shaft sleeve, 303d-Outlet pipe, 303d-1-Flow-fixing pipe sleeve, 303d-2-Flow-fixing plate. Detailed Implementation

[0024] The technical solutions of the present invention will be clearly and completely described below with reference to the accompanying drawings of the embodiments of the present invention.

[0025] Example 1

[0026] Please see Figures 1 to 3 This utility model is a filtration device for removing impurities from electroplating solution, including a water pump 1, a coarse filter component 2, and an impurity removal component 3. The impurity removal component 3 includes an impurity removal liquid loop pipe 301, a loop pipe sleeve 302, and a mixing component 303. By setting the coarse filter component 2 at the outlet end of the water pump 1 and the impurity removal component 3 at the outlet end of the coarse filter component 2, the water pump 1 pumps the electroplating solution into the coarse filter component 2 to filter and remove solid particulate impurities in the electroplating solution. The electroplating solution after filtering out solid particulate impurities flows into the impurity removal component 3, and an impurity removal agent is added to the electroplating solution through the impurity removal liquid loop pipe 301 in the impurity removal component 3. The electroplating solution after adding the impurity removal agent is discharged back into the electroplating tank and energized, thereby removing metal ion impurities in the electroplating solution.

[0027] Specifically, the impurity removal liquid ring pipe 301 is sleeved inside the ring pipe sleeve 302. The outer wall of the impurity removal liquid ring pipe 301 is connected to the inlet pipe 301a, which penetrates the ring pipe sleeve 302. A set of outlet holes 301b are circumferentially arrayed through the inner ring wall of the impurity removal liquid ring pipe 301. The mixing component 303 is located at the outlet of the lower end of the ring pipe sleeve 302. The coarse filter component 2 is located at the upper end of the ring pipe sleeve 302. The lower outlet end of the water pump 1 is connected to the upper end of the coarse filter component 2.

[0028] Furthermore, the coarse filter component 2 includes a coarse filter basket 201 and a basket sleeve 202. The lower end of the basket sleeve 202 is connected to the annular sleeve 302, and the upper end of the basket sleeve 202 is connected to the lower outlet end of the water pump 1 through a flange. The coarse filter basket 201 is a tube structure with an open upper end and a closed lower end. A set of coarse filter basket holes 201a are provided through the side wall and bottom of the coarse filter basket. A threaded sleeve 201b is fixed on the upper outer wall of the coarse filter basket 201. The threaded sleeve 201b is screwed into the upper inner wall of the basket sleeve 202. When the plating solution passes through the coarse filter basket holes 201a, it filters out solid impurity particles and retains them in the coarse filter basket 201.

[0029] The operation process in this embodiment is as follows:

[0030] Pump 1 pumps the electroplating solution from the electroplating tank into the coarse filter basket 202. When the electroplating solution passes through the coarse filter basket hole 201a, solid impurity particles are filtered and retained in the coarse filter basket 201. The electroplating solution after filtration through the coarse filter basket 202 enters the ring tube 302. The impurity removal solution enters the impurity removal solution ring tube 301 from the inlet pipe 301a and flows out from the outlet hole 301b, entering the electroplating solution flowing into the impurity removal solution ring tube 301. After being mixed by the mixing component, it is discharged back into the electroplating tank and energized to remove metal impurity ions from the electroplating solution.

[0031] Example 2

[0032] Please see Figures 1 to 5 Based on Example 1, the mixing component 303 includes a converging sleeve 303a, a rotating paddle 303b, and a rotating shaft seat 303c. By installing the converging sleeve 303a at the lower end of the annular sleeve 202, when the electroplating solution with added impurity remover flows into the converging sleeve 303a, it drives the rotating paddle 303b to rotate, thereby making the electroplating solution and the added impurity remover fully mixed.

[0033] Specifically, the convergence sleeve 303a is sleeved on the lower end of the annular sleeve 302, and the rotating shaft seat 303c is threaded onto the inner wall of the lower end of the convergence sleeve 303a. A set of connecting arms 303c-1 are fixedly arranged in a circumferential array on the inner wall of the rotating shaft seat 303c. A rotating shaft sleeve 303c-2 is fixedly provided at the end of each connecting arm 303c-1 away from the rotating shaft seat 303c. A rotating shaft 303b-1 is fixedly provided at the lower end of the rotating paddle 303b, and the rotating shaft 303b-1 is rotatably installed in the rotating shaft sleeve 303c-2.

[0034] Furthermore, a stirring paddle sleeve 303b-2 is threaded onto the outer side of one end of the rotating shaft 303b-1 that passes through the rotating shaft sleeve 303c-2. A set of stirring paddles 303b-3 are fixedly arranged in a circumferential array on the outer side wall of the stirring paddle sleeve 303b-2. When the electroplating solution passes through the rotating paddle 303b, it drives the rotating paddle 303b to rotate, which in turn drives the stirring paddles 303b-3 to rotate, thus mixing the electroplating solution with the impurity removal agent.

[0035] Furthermore, the converging sleeve 303a is integrally formed from top to bottom by an inlet section 303a-1, a converging section 303a-2, and an outlet section 303a-3. The converging section 303a-2 gradually converges downwards, and the rotating shaft seat 303c is threaded onto the inner wall of the outlet section 303a-3. The electroplating solution enters from the inlet section 303a-1, and after being converged by the converging section 303a-2, its flow rate increases, and then it flows out from the outlet section 303a-3, driving the rotating paddle 303b to rotate.

[0036] Furthermore, the outer wall of the outlet section 303a-3 is threaded with a liquid outlet pipe 303d, and the agitator 303b-3 is fitted onto the inner wall of the liquid outlet pipe 303d.

[0037] Furthermore, a flow-regulating sleeve 303d-1 is fixedly sleeved on the inner wall of the outlet pipe 303d. The flow-regulating sleeve 303d-1 is a tubular structure with openings at both the top and bottom. Flow-regulating plates 303d-2 are fixedly arranged in a circumferential array on the inner wall of the flow-regulating sleeve 303d-1. The surface of the flow-regulating plates 303d-2 is perpendicular to the pipe axis of the flow-regulating sleeve 303d-1. After the electroplating solution flows into the flow-regulating sleeve 303d-1, the eddy current generated by the rotation of the stirring paddle 303b disappears under the action of the flow-regulating plates 303d-2.

[0038] The operation process in this embodiment is as follows:

[0039] The electroplating solution enters from the inlet section 303a-1 and is accelerated after being constricted by the converging section 303a-2. It then flows out from the outlet section 303a-3. When the electroplating solution passes through the rotating paddle 303b, it drives the rotating paddle 303b to rotate, which in turn drives the stirring paddle 303b-3 to rotate, thus mixing the electroplating solution with the impurity remover. After the electroplating solution flows into the constant flow tube sleeve 303d-1, the eddies generated by the rotation of the stirring paddle 303b disappear under the action of the constant flow plate 303d-2. Furthermore, the eddies collide with the constant flow plate 303d-2, further mixing the impurity remover with the electroplating solution.

[0040] In the description of this specification, references to terms such as "an embodiment," "example," "specific example," etc., indicate that a specific feature, structure, material, or characteristic described in connection with that embodiment or example is included in at least one embodiment or example of the present invention. In this specification, the illustrative expressions of the above terms do not necessarily refer to the same embodiment or example. Furthermore, the specific features, structures, materials, or characteristics described may be combined in any suitable manner in one or more embodiments or examples.

Claims

1. An electroplating solution impurity removing filter device comprising a water pump (1), a rough filter part (2) and an impurity removing part (3), characterized in that: The impurity removal component (3) includes an impurity removal liquid ring pipe (301), a ring pipe sleeve (302), and a mixing component (303). The impurity removal liquid ring pipe (301) is sleeved inside the ring pipe sleeve (302). The outer wall of the impurity removal liquid ring pipe (301) is connected to an inlet pipe (301a). The inlet pipe (301a) penetrates the ring pipe sleeve (302). A set of outlet holes (301b) are circumferentially arrayed through the inner wall of the impurity removal liquid ring pipe (301). The mixing component (303) is located at the outlet of the lower end of the ring pipe sleeve (302). The coarse filter component (2) is located at the upper end of the ring pipe sleeve (302). The lower outlet end of the water pump (1) is connected to the upper end of the coarse filter component (2).

2. The impurity removal filter device for electroplating solution according to claim 1, characterized in that: The coarse filter component (2) includes a coarse filter basket (201) and a basket sleeve (202). The lower end of the basket sleeve (202) is connected to the ring sleeve (302). The upper end of the basket sleeve (202) is connected to the lower outlet end of the water pump (1) through a flange. The coarse filter basket (201) is a tube structure with an open upper end and a closed lower end. A set of coarse filter basket holes (201a) are provided through the side wall and bottom of the coarse filter basket. A threaded sleeve (201b) is fixed on the upper outer wall of the coarse filter basket (201). The threaded sleeve (201b) is screwed into the upper inner wall of the basket sleeve (202).

3. The impurity removal filter device for electroplating solution according to claim 1, characterized in that: The mixing component (303) includes a convergence sleeve (303a), a rotating propeller (303b), and a rotating shaft seat (303c). The convergence sleeve (303a) is sleeved on the lower end of the annular sleeve (302). The rotating shaft seat (303c) is threaded onto the inner wall of the lower end of the convergence sleeve (303a). A set of connecting arms (303c-1) is circumferentially arrayed and fixed on the inner wall of the rotating shaft seat (303c). A rotating shaft sleeve (303c-2) is fixed at the end of each connecting arm (303c-1) away from the rotating shaft seat (303c). A rotating shaft (303b-1) is fixed at the lower end of the rotating propeller (303b). The rotating shaft (303b-1) is rotatably mounted inside the rotating shaft sleeve (303c-2).

4. The impurity removal filter device for electroplating solution according to claim 3, characterized in that: The rotating shaft (303b-1) passes through the outer side of the rotating shaft sleeve (303c-2) and is threaded with the stirring paddle sleeve (303b-2). A set of stirring paddles (303b-3) are fixedly arranged in a circumferential array on the outer side wall of the stirring paddle sleeve (303b-2).

5. The impurity removal filter device for electroplating solution according to claim 4, characterized in that: The converging sleeve (303a) is integrally formed from top to bottom by an inlet section (303a-1), a converging section (303a-2), and an outlet section (303a-3). The converging section (303a-2) gradually converges downwards, and the rotating shaft seat (303c) is threaded onto the inner wall of the outlet section (303a-3).

6. The impurity removal filter device for electroplating solution according to claim 5, wherein: The outer wall of the outlet section (303a-3) is threaded with a liquid outlet pipe (303d), and the stirring paddle (303b-3) is sleeved on the inner wall of the liquid outlet pipe (303d).

7. The impurity removal filtration device for electroplating solution according to claim 6, characterized in that: The inner wall of the outlet pipe (303d) is fixedly sleeved with a flow-regulating sleeve (303d-1). The flow-regulating sleeve (303d-1) is a tubular structure with openings at both the top and bottom. Flow-regulating plates (303d-2) are fixedly arranged in a circumferential array on the inner wall of the flow-regulating sleeve (303d-1). The surface of the flow-regulating plates (303d-2) is perpendicular to the pipe axis of the flow-regulating sleeve (303d-1).

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