CN214400791U

CN214400791U - Electroplating pool

Info

Publication number: CN214400791U
Application number: CN202120312746.1U
Authority: CN
Inventors: 潘莉美
Original assignee: Shanghai Jinxia Industrial Co ltd
Current assignee: Shanghai Jinxia Industrial Co ltd
Priority date: 2021-02-03
Filing date: 2021-02-03
Publication date: 2021-10-15
Anticipated expiration: 2031-02-03

Abstract

The utility model relates to an electroplating pool relates to the field of electroplating technique, and it includes total cell body, and total cell body divides into a plurality of minutes cell bodies, has placed different electrolyte in every minute cell body, is provided with the splash shield on the total cell body inner wall, and the splash shield is located and is close to total cell body open-ended one end, is provided with the baffle between per two adjacent minute cell bodies, and the tip of baffle also is provided with the splash shield. The electrolyte can be reduced from being splashed into the other sub-tank from one sub-tank, and therefore mixing of the electrolyte in different sub-tanks is reduced.

Description

Electroplating pool

Technical Field

The application relates to the field of electroplating technology, in particular to an electroplating pool.

Background

Electroplating is a process of plating a thin layer of other metals or alloys on the surface of some metals by using the principle of electrolysis, and is a process of attaching a layer of metal film on the surface of a metal or other material product by using the action of electrolysis, thereby having the effects of preventing metal oxidation (such as corrosion), improving wear resistance, conductivity, light reflection, corrosion resistance (such as copper sulfate and the like), enhancing the appearance and the like.

When a plurality of layers of metal are required to be plated on the surface of the metal, a plurality of different electrolytes are often placed in adjacent electroplating baths, and then the metal is sequentially placed in the plurality of different electrolytes for electroplating.

In view of the above-mentioned related art, the inventor believes that when the metal to be plated is large in volume or mass, the electrolyte may be sputtered when the metal to be plated is placed in one of the plating baths, which not only easily causes mixing of the electrolyte, but also may be sputtered to workers.

SUMMERY OF THE UTILITY MODEL

In order to reduce the sputtering of electrolyte when putting into the electroplating bath with waiting to plate the metal, reduce the mixture of electrolyte, the application provides an electroplating bath.

The application provides an electroplating pool, adopts following technical scheme:

the utility model provides an electroplating pool, includes total cell body, total cell body divide into a plurality of minute cell bodies, every different electrolytes have been placed in minute cell body, be provided with the splash shield on the total cell body inner wall, the splash shield is located and is close to total cell body open-ended one end, every two is adjacent divide to be provided with the baffle between the cell body, the tip of baffle also is provided with the splash shield.

Through adopting above-mentioned technical scheme, when placing the great metal of treating of volume or quality in dividing the cell body, divide the electrolyte in the cell body to block by splash shield and baffle, the baffle can make electrolyte be difficult for following one of them and divide the cell body internal splash to another in, has reduced the mixture of the internal electrolyte of different branch cells, and the splash shield also can make electrolyte be difficult for the splash to staff on one's body, also can effectively ensure staff's safety.

Optionally, the height of the baffle is higher than that of the total tank body.

By adopting the technical scheme, the effect that the baffle blocks the electrolyte sputtering is enhanced.

Optionally, the baffle is fixedly connected with an inclined plate, and the inclined plate and the baffle are in an L shape.

By adopting the technical scheme, when the metal to be plated is taken out of one sub-tank body, the electrolyte arranged in the sub-tank body at the position can be attached to the metal to be plated, the attached electrolyte can drip on the inclined plate at the moment, and then the electrolyte flows back to the sub-tank body at the position along the inner wall of the inclined plate, so that the mixing of the electrolyte in the sub-tank body can be reduced.

Optionally, the inner wall of the inclined plate is smoothly arranged, and a chamfer is arranged at the joint of the inclined plate and the baffle.

Through adopting above-mentioned technical scheme, can make the electrolyte that drops on the hang plate change into flow into the branch cell at place in, improve the utilization ratio of electrolyte.

Optionally, the baffle sets up a plurality ofly, a plurality ofly the baffle fixed connection, a plurality of fixed connection the baffle is last to have seted up the catch basin.

Through adopting above-mentioned technical scheme, taking out in the branch pond to the metal of waiting to plate from one, can be stained with the electrolyte of placing in the branch pond that attaches the place on the metal of waiting to plate, before moving to next branch pond in and electroplate, the electrolyte that is stained with at this moment and attaches will drip in the collecting tank to can reduce the mixture of the internal electrolyte of branch pond.

Optionally, the baffle is detachably connected with a storage hopper, and an opening of the storage hopper and an opening of the liquid collecting tank are communicated with each other.

Through adopting above-mentioned technical scheme, accomodate the fill and can be convenient for collect and wait to plate the electrolyte that is stained with on the metal and attach, collect electrolyte in the collecting tank.

Optionally, one end of the storage hopper, which is far away from the baffle, is flared.

Through adopting above-mentioned technical scheme, increased the bore of accomodating the fill, it is more convenient to make to accomodate the fill and collect the electrolyte that drips, has improved the utilization ratio of electrolyte.

Optionally, each sub-tank body is internally provided with a filter screen, each sub-tank body is provided with a hook on the side wall, and the filter screens are hung on the hooks.

Through adopting above-mentioned technical scheme, the filter screen can be collected impurity and the residue that the electrolysis in-process produced, can reduce because of impurity and the condition that the residue blockked up the leakage fluid dram, is convenient for change the waste liquid, and the filter screen is hung on the inner wall of branch cell body, convenient to detach and installation filter screen to in time clear up impurity and residue, do not influence the waste liquid of discharging.

Optionally, the bottom of the filter screen is fixedly connected with a filter plate, and the size of the filter hole of the filter plate is smaller than that of the filter hole of the filter screen.

Through adopting above-mentioned technical scheme, filter plate and filter screen cooperation are used, have played dual filterable effect, and the filter screen is used for filtering great impurity, and the filter plate filters less impurity, makes the difficult leakage fluid dram that blocks up of granular impurity of little.

Optionally, the total cell body includes the washing pond, it sets up in the outside to wash the pond one side of minute cell body, place cleaning solution in the washing pond, the metal that treats plate passes through after wasing the pond, pass through every divide the cell body to electroplate.

By adopting the technical scheme, the surface of the metal to be plated can be cleaned before electroplating, so that impurities such as dust, oil stains and the like adhered to the surface of the metal to be plated can not be brought into the sub-tank body.

In summary, the present application includes at least one of the following beneficial technical effects:

the electrolyte is not easy to splash from one sub-tank body into the other sub-tank body, so that the mixing of the electrolyte in different sub-tank bodies is reduced, and the electrolyte is not easy to splash onto the bodies of workers, so that the safety of the workers can be effectively guaranteed;

the electrolyte adhered to the surface of the metal to be plated can be collected and recovered, so that the waste of the electrolyte is reduced, and the utilization rate of the electrolyte is improved;

can effectively reduce the blockage of the liquid outlet of the electroplating pool caused by impurities and residues generated in the electroplating process.

Drawings

FIG. 1 is a schematic view of the overall structure of embodiment 1 of the present application;

FIG. 2 is a schematic diagram showing the construction of a filter screen and a filter plate;

fig. 3 is a schematic view of the overall structure of embodiment 2 of the present application.

Reference numerals: 1. a main tank body; 2. a separation tank body; 3. a baffle plate; 4. a splash shield; 5. an inclined plate; 6. chamfering; 7. hooking; 8. filtering with a screen; 9. filtering the plate; 10. a cleaning tank; 11. a liquid collecting tank; 12. a storage bucket.

Detailed Description

The present application is described in further detail below with reference to figures 1-3.

The embodiment of the application discloses an electroplating pool.

Example 1:

referring to fig. 1, the electroplating tank includes a main tank body 1, and the whole main tank body 1 is rectangular. The main tank body 1 comprises a plurality of sub-tank bodies 2, and a baffle 3 is arranged between every two sub-tank bodies 2. The thickness of the baffle 3 is thicker than the side wall of the total cell body 1, and the height of the baffle 3 is higher than the height of the total cell body 1. Baffle 3 can be effectively with two adjacent minute cell bodies 2 separate to when placing the metal of treating that volume or quality are great in minute cell body 2, divide the electrolyte in the cell body 2 to be blockked by baffle 3, baffle 3 can make electrolyte be difficult for sputtering to another minute cell body 2 from one of them minute cell body 2 in, thereby reduce the mixture of the interior electrolyte of different minute cell bodies 2. The side wall edge of the main tank body 1 is integrally provided with or welded with a splash guard 4, and the splash guard 4 is arranged at the opening part close to the main tank body 1. The splash guard 4 can reduce effectively and wait to plate the sputter of electrolyte when metal, can reduce the mixture of electrolyte in the different minute cell bodies 2 on the one hand, and on the other hand can reduce the spill of electrolyte, makes the difficult sputter of electrolyte work personnel on one's body, has ensured the security that the work personnel electroplate the work effectively.

The top of the baffle 3 is integrally provided with or welded with an inclined plate 5, the inclined plate 5 is obliquely arranged and is L-shaped with the baffle 3, and the included angle between the inclined plate 5 and the baffle 3 is 120-135 degrees. When the metal to be plated is taken out of one sub-tank body 2, the metal to be plated is adhered with the electrolyte arranged in the sub-tank body 2, and the adhered electrolyte drops on the inclined plate 5 and then flows back into the sub-tank body 2 along the inner wall of the inclined plate 5, so that the mixing of the electrolyte in the sub-tank body 2 can be reduced. The surface of the inclined plate 5 is smooth, and the connecting part of the inclined plate 5 and the baffle 3 is provided with a chamfer 6, so that the electrolyte dropping on the inclined plate 5 can more easily flow into the sub-tank 2, and the utilization rate of the electrolyte is improved.

Referring to fig. 1 and 2, a hook 7 is fixed on the inner wall of the separation tank body 2 by gluing, welding or threads. The filter screen 8 is hung on the hook 7, the whole filter screen 8 is in a cuboid shape, and the size of the filter screen 8 is smaller than the inner diameter of the sub-tank body 2. Filter screen 8 can be collected the impurity and the residue that produce among the electrolysis process, can reduce because of impurity and the condition that the residue blockked up the leakage fluid dram, is convenient for change the waste liquid, and filter screen 8 hangs on the inner wall of branch cell body 2, convenient to detach and installation filter screen 8 to in time clear up impurity and residue, do not influence the discharge waste liquid. The bottom of the filter screen 8 is provided with a filter plate 9, and the size of the filter holes on the filter plate 9 is smaller than that of the filter holes of the filter screen 8. The filter plate 9 and the filter screen 8 are matched for use, so that a double-filtering effect is achieved, the filter screen 8 is used for filtering large impurities, the filter plate 9 filters small impurities, and the small granular impurities are not prone to blocking a liquid outlet.

Referring to fig. 1, the total cell body 1 further includes a washing tank 10, and the washing tank 10 is located at one side of the sub cell body 2 at the outer side. The cleaning pool 10 is used for containing cleaning solution, before electroplating, to-be-plated metal can be placed in the cleaning pool 10, dust and oil stains on the surface of the to-be-plated metal are cleaned, and then the cleaned to-be-plated metal is placed in the sub-pool body 2 for electroplating. This can effectively reduce the contamination of the electrolyte in the split cell body 2.

The implementation principle of an electroplating pool in embodiment 1 of the application is as follows: firstly, the metal to be plated is placed in a cleaning tank 10, and is placed in a sub-tank body 2 for electroplating after being cleaned. When the volume and the mass of the metal to be plated are large, the baffle 3 can effectively reduce the phenomenon that the electrolyte is sputtered into the other sub-tank body 2 from one sub-tank body 2, and the inclined plate 5 can enable the electrolyte attached to the metal to be plated to flow back into the sub-tank body 2 again, so that the mixing of the electrolytes in different sub-tank bodies 2 can be reduced, and the waste of the electrolyte is reduced. The anti-splash plate 4 effectively reduces the splashing of the electrolyte when the metal to be plated is put in, can effectively reduce the mixing of the electrolyte and can also reduce the splashing of the electrolyte to workers.

Example 2:

referring to fig. 3, the present embodiment is different from embodiment 1 in that the baffle 3 is thicker than that of embodiment 1, the baffle 3 is provided with a liquid collecting groove 11, and the depth of the liquid collecting groove 11 is equivalent to that of each cell body 2. When the metal to be plated is taken out of one sub-tank body 2, all the electrolyte arranged in the sub-tank body 2 can be attached to the metal to be plated, and before the metal to be plated is moved into the next sub-tank body 2 for electroplating, the attached electrolyte can drop into the liquid collecting tank 11, so that the mixing of the electrolyte in the sub-tank body 2 can be reduced. The top of the baffle 3 is connected with a containing bucket 12 in a threaded manner or in a clamping manner, the opening of the containing bucket 12 is communicated with the opening of the collecting tank 11, and the containing bucket 12 is flared upwards. So increased and accomodate the bore of fill 12, made to accomodate fill 12 and collected the electrolyte that drips more convenient, improved the utilization ratio of electrolyte.

The implementation principle of an electroplating pool in embodiment 2 of the application is as follows: when the metal to be plated is taken out of one of the sub-tank bodies 2, the electrolyte attached to the metal to be plated can drop into the liquid collecting tank 11, so that the mixing of the electrolyte can be effectively reduced, the waste of the electrolyte is reduced, and the utilization rate of the electrolyte is improved.

The above embodiments are preferred embodiments of the present application, and the protection scope of the present application is not limited by the above embodiments, so: all equivalent changes made according to the structure, shape and principle of the present application shall be covered by the protection scope of the present application.

Claims

1. The utility model provides an electroplating pool, includes total cell body (1), total cell body (1) divide into a plurality of minute cell bodies (2), every different electrolyte, its characterized in that have been placed in minute cell body (2): be provided with splash guard (4) on total cell body (1) inner wall, splash guard (4) are located and are close to total cell body (1) open-ended one end, and every two are adjacent be provided with baffle (3) between branch cell body (2), the tip of baffle (3) also is provided with splash guard (4).

2. The plating cell of claim 1, wherein: the height of the baffle (3) is higher than that of the main tank body (1).

3. The plating cell of claim 2, wherein: baffle (3) fixedly connected with hang plate (5), hang plate (5) with be "L" type between baffle (3).

4. The plating cell of claim 3, wherein: the inner wall of the inclined plate (5) is smoothly arranged, and a chamfer (6) is arranged at the joint of the inclined plate (5) and the baffle (3).

5. The plating cell of claim 1, wherein: the baffle (3) is provided with a plurality of baffles (3) which are fixedly connected, and a liquid collecting tank (11) is arranged on the baffles (3) which are fixedly connected.

6. The plating cell of claim 5, wherein: the baffle (3) is detachably connected with a containing bucket (12), and an opening of the containing bucket (12) is communicated with an opening of the liquid collecting tank (11).

7. The plating cell of claim 6, wherein: one end of the storage hopper (12) far away from the baffle (3) is in a flaring shape.

8. The plating cell of claim 1, wherein: each of the sub-tank bodies (2) is internally provided with a filter screen (8), each of the side walls of the sub-tank bodies (2) is provided with a hook (7), and the filter screen (8) is hung on the hook (7).

9. The plating cell of claim 8, wherein: the bottom fixedly connected with filter plate (9) of filter screen (8), the filtration pore size of filter plate (9) is less than the filtration pore size of filter screen (8).

10. The plating cell of claim 1, wherein: the total pool body (1) comprises a cleaning pool (10), the cleaning pool (10) is arranged on one side of the sub-pool body (2) on the outer side, cleaning solution is placed in the cleaning pool (10), and metal to be plated passes through the cleaning pool (10) and then passes through each sub-pool body (2) for electroplating.