CN202830213U - Plating solution circulation filtration system - Google Patents
Plating solution circulation filtration system Download PDFInfo
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- CN202830213U CN202830213U CN 201220397326 CN201220397326U CN202830213U CN 202830213 U CN202830213 U CN 202830213U CN 201220397326 CN201220397326 CN 201220397326 CN 201220397326 U CN201220397326 U CN 201220397326U CN 202830213 U CN202830213 U CN 202830213U
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- electroplating solution
- plating tank
- plating
- filter vat
- circulated throughout
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Abstract
The utility model provides a plating solution circulation filtration system. The plating solution circulation filtration system comprises a plurality of plating tanks provided with input pipelines and output pipelines, a plurality of circulation filtration pumps and filtration tanks. The filtration tanks are mutually communicated with the plurality of plating tanks through the input pipelines and the output pipelines. The circulation filtration pumps control circulation of plating solutions among the plurality of plating tanks, the input pipelines, the output pipelines and the filtration tanks. The plating solution circulation filtration system simplifies equipment, ensures product reliability degree, and reduces cost.
Description
Technical field
The utility model relates to a kind of electroplating technology system, relates in particular to the electroplating solution of cyclic filtering system in a kind of electroplating technology.
Background technology
Plating be mainly used to improve product corrosion stability, wear resistance, decorate or make product have certain function, it is widely used.
In order to guarantee the quality of coating, except the processing parameters such as strict control temperature, current density, PH, also the factors such as impurity in necessary attention stirring and the electroplate liquid are on the impact of plating quality, in order to prevent the concentration polarization of bubble when coating surface is detained and electroplate, usually adopt the mode of mechanical stirring or pneumatic blending, or adopt the circular flow mode to promote the circulation of electroplate liquid.It is one of important measures that guarantee the plated item quality that electroplating solution filters.
A kind of electroplating technology production line of prior art structure as shown in Figure 1.Described electroplating technology production line 1 is used for the plating piece product (not shown) of electroplated is electroplated processing in plating tank 10.Described electroplating technology production line 1 comprises a plurality of plating tanks 10, a plurality of filter vat 11, a plurality of filter pump 13 and Controlling System 15 of being circulated throughout.
The adjacent setting that is parallel to each other of described a plurality of plating tank 10.Described a plurality of filter vat 11 same parallel adjacent settings.Each plating tank 10 forms one group of electroplating solution of cyclic filtering system with corresponding contiguous settings of a filter vat 11 wherein.In each electroplating solution of cyclic filtering system, each plating tank 10 and a wherein filter vat 11 contiguous settings.And realize interconnecting by input and output pipeline 17.
Describedly be circulated throughout filter pump 13 and described Controlling System 15 corresponding electrical connections.Described Controlling System 15 produces to control signal to and describedly is circulated throughout filter pump 13, and drive described be circulated throughout filter pump 13 carry plating bath in the described plating tank 11 to the described filter vat 11 to process.Simultaneously, the described filter pump 13 same extremely described plating tank 10 realization electroplating technology needs of electroplate liquid of carrying in the described filter vat 11 that are circulated throughout.
Thus, realize that the plating bath between described plating tank 10 and the described filter vat 11 circulates.
Yet, in above-mentioned electroplating technology production line structure 1, described plating tank 10 need to form one group of electroplating solution of cyclic filtering system with corresponding contiguous settings of a filter vat 11 wherein, independently filter vat 11 is corresponding with it in requisition for arranging one to that is to say 10 pairs of each plating tanks, so so that whole electroplating technology production line complex structure, floor space is large, increases the management and control cost.
On the other hand, because in the electroplating technology, because the chemistry of function electrolytic coating and the improvement of physicals, so that the requirement of the chemical concentration of filter operation and filtrate occurs significantly to change.Often comprise separate many groups electroplating solution of cyclic filtering system in the existing electroplating technology production line structure 1, be subjected to appointed condition and manual operation differentia influence, the bath concentration that is difficult to accomplish the electroplating solution of cyclic filtering system of different groups reaches unanimity, so cause the effect after plating piece product to be plated is electroplated uneven, reduce the electroplating technology reliability.
Given this, how to improve electroplating device to the reliability of plating piece, reduce device resource and the management and control cost is the industry problem demanding prompt solution.
The utility model content
For the filtration of prior art plating bath management disunity, the plating piece quality product is uneven, equipment is numerous and diverse and cost is high technical problem, the utility model provide a kind of to the plating bath unified management, the plating piece production reliability is high and economize on resources, the plating fluid circulating system of simplified apparatus, reduction cost is real in necessary.
A kind of electroplating solution of cyclic filtering system, it comprises the plating tank of a plurality of tool input channels and output channel, a plurality of filter pump and filter vat of being circulated throughout, described filter vat and a plurality of plating tank connect mutually by described input channel and output channel, and the described filter pump that is circulated throughout is controlled described electroplate liquid and circulated between described a plurality of plating tanks, described input channel, described output channel and described filter vat.
As the further improvement of above-mentioned electroplating solution of cyclic filtering system, input channel one end of described plating tank and described plating tank internal run-through, the other end and described filter vat connect with each other.
As the further improvement of above-mentioned electroplating solution of cyclic filtering system, described output channel one end and described plating tank internal run-through, the other end and described filter vat connect with each other.
As the further improvement of above-mentioned electroplating solution of cyclic filtering system, the input channel of adjacent plating tank and output channel are connected in series setting mutually.
Further improvement as above-mentioned electroplating solution of cyclic filtering system, the described filter pump that is circulated throughout comprises that first is circulated throughout filter pump and second and is circulated throughout filter pump, described first is circulated throughout filter pump closes on the setting of described input channel side, and described second is circulated throughout filter pump closes on the setting of described output channel side.
As the further improvement of above-mentioned electroplating solution of cyclic filtering system, described electroplating solution of cyclic filtering system also comprises the cycle control module, and described cycle control module is circulated throughout the corresponding electrical connection of filter pump and arranges with described.
As the further improvement of above-mentioned electroplating solution of cyclic filtering system, described cycle control module produces the first control signal and controls described the first circulating filtration pump work, and described first is circulated throughout filter pump orders about electroplate liquid and be circulated to described filter vat from described plating tank.
As the further improvement of above-mentioned electroplating solution of cyclic filtering system, described cycle control module produces the second control signal and controls described the second circulating filtration pump work, and described second is circulated throughout filter pump orders about electroplate liquid and be circulated to described plating tank from described filter vat.
As the further improvement of above-mentioned electroplating solution of cyclic filtering system, described filter vat is folded between the described plating tank.
As the further improvement of above-mentioned electroplating solution of cyclic filtering system, described input channel and described output channel are to adopt plastic cement material to process.
Compared to prior art, in the electroplating solution of cyclic filtering of the present utility model system, single filter vat is set to be connected mutually with described a plurality of plating tanks simultaneously, and the described electroplate liquid of unified filtration treatment, unified management, the concentration that guarantees plating bath is consistent, effectively solves the inconsistent uneven defectives of plating piece effect that cause of parameter such as existing bath concentration, improves production reliability.Simultaneously, reduce to use a plurality of filter vat, simplied system structure, reduce number of devices, reduce the volume of whole production technique, simplify the operation, reduce the cost.
Description of drawings
Fig. 1 is the floor map of a kind of electroplating technology production line of prior art structure.
Fig. 2 is the floor map that the utility model the first embodiment discloses the electroplating solution of cyclic filtering system architecture.
Fig. 3 is the perspective exploded view that plating tank shown in Figure 2 is connected with filter vat.
Fig. 4 is the floor map that the utility model the second embodiment discloses the electroplating solution of cyclic filtering system architecture.
Embodiment
Below in conjunction with accompanying drawing the utility model is elaborated.
Seeing also Fig. 2, is the floor map that the utility model discloses a kind of electroplating solution of cyclic filtering system the first embodiment.Described electroplating solution of cyclic filtering system 3 comprises a plurality of plating tanks 31, filter vat 33, is circulated throughout filter pump 35 and cycle control module 37.
Described plating tank 31 in order to the splendid attire electroplate liquid to realize the electroplating activity to unplated piece.Described a plurality of plating tank 31 is parallel adjacent spread configuration.
Each plating tank 31 comprises receiving space 311, input channel 313 and the output channel 315 of accommodating plating bath, specifically as shown in Figure 3.Input and output that described input channel 313 and described output channel 315 are realized the electroplate liquid of accommodating in plating tank 31 receiving spaces 311.The receiving space of described input channel 313 1 ends and described plating tank 311 connects mutually, and the other end then connects mutually with described filter vat 33.Described output channel 315 same ends and described plating tank 31 connect mutually, mutually connect with described filter vat 33 and the other end is same.Described input channel 313 all is to adopt the plastic material of acid-alkali-corrosive-resisting to process with described output channel 315.
Described filter vat 33 is folded between the described plating tank 31, and with the setting that is arranged in array of described a plurality of plating tanks 31.Directly realize mutually connecting by described input channel 313 and output channel 315 respectively between described filter vat 33 and each plating tank 31.
The described filter pump 35 that is circulated throughout is separately positioned on described input channel 313 sides and described output channel 315 sides, it provides pressure-acting in described plating bath, and order about described plating bath from described plating tank 31 through described output channel 315 to described filter vat 33, perhaps order about after the filtration plating bath from described filter vat 33 through described input channel 313 to described plating tank 31.In the present embodiment, the filter pump 35 that is circulated throughout that is arranged on described input channel 313 sides is first to be circulated throughout filter pump 351; The filter pump 35 that is circulated throughout that is arranged on described output channel 315 sides is second to be circulated throughout filter pump 353.
Described cycle control module 37 is circulated throughout the corresponding electrical connections of filter pump 35 and arranges with described, and it control the described working order that is circulated throughout filter pump 35, and it produces the described filter pump 35 that is circulated throughout of drive and works.Particularly, described cycle control module 37 produces the first control signal and drives described first and be circulated throughout filter pump 351 work, order about electroplate liquid in the described plating tank 31 through described output channel 315 to described filter vat 33.Described cycle control module 37 produce the second control signal drive described second be circulated throughout filter pump 353 order about electroplate liquid in the described filter vat 33 through described input channel 313 to described plating tank 31.So, form electroplating solution of cyclic filtering system 3.
When 3 work of described electroplating solution of cyclic filtering system, it comprises the steps:
Step S1, described cycle control module 37 produces the first drive control signal and extremely described first is circulated throughout filter pump 351.
Step S2, described first is circulated throughout filter pump 351 under described the first drive control signal effect, order about electroplate liquid in the described plating tank 31 through described output channel 315 to described filter vat 33.
Step S3, described electroplate liquid form qualified electroplate liquid after processing after filtration in described filter vat 33.
Step S4, described second is circulated throughout the second drive control signal that filter pump 353 receives described cycle control module 37 again, described second is circulated throughout filter pump 353 under described the second drive control signal effect, order about electroplate liquid in the described filter vat 33 through described input channel 313 to the receiving space 311 of described plating tank 31.
So far, realize the circulation of described electroplate liquid in the plating tank 31 of described electroplating solution of cyclic filtering system 3 and described filter vat 33.In this working cycle, correspondence is qualified electroplate liquid in the receiving space of described plating tank 31, and it can carry out electroplating technology to the plating piece product of electroplated.33 pairs of described filter vat are contaminated or contain after the defective plating of impurity solution and carry out filtration treatment and form qualified electroplate liquid, process or the concentration adjustment processing of electroplating solution etc. such as: carbon adsorption filtration.
When the electroplate liquid in the described plating tank 31 contains impurity etc. and becomes defective electroplate liquid, 3 work of described electroplating solution of cyclic filtering system, described defective electroplate liquid is in described plating tank 31 is circulated to described filter vat 33.Simultaneously, the qualified electroplate liquid after the processing then in described filter vat 33 is circulated to the receiving space 311 of described plating tank 31, guarantees that the electroplate liquid in the described plating tank 31 is up to standard, reduces simultaneously the loss of plating bath, improves the plating bath utilization ratio, economizes on resources, and reduces the cost.
In the present embodiment, described filter vat 33 is set to be folded between the described plating tank 31, position relationship between wherein said filter vat 33 and the described plating tank 31, can also be apart from the equal consistent position of the distance between each plating tank 31, or the distance described each plating tank 31 between the position the shortest apart from sum, every be intended to form between described a plurality of plating tank 31 and between the filter vat 33 the electroplating solution of cyclic filtering system architecture of mutual circulation all belong to aim of the present utility model.
Certainly, further improvement as above-mentioned embodiment, the quantity of described filter vat 33 can be according to the technique of producing line or the corresponding adjustment of place needs, but mutually connect between described a plurality of plating tank 31 and the described filter vat 33, plating bath circulates between different plating tank 31 and filter vat 33.
Compared to prior art, in electroplating solution of cyclic filtering of the present utility model system 3, single filter vat 33 is set to be connected mutually with described a plurality of plating tanks 31 simultaneously, and the described electroplate liquid of unified filtration treatment, unified management, the concentration that guarantees plating bath is consistent, effectively solves the inconsistent uneven defectives of plating piece effect that cause of parameter such as existing bath concentration, improves production reliability.Simultaneously, reduce to use a plurality of filter vat 33, simplied system structure, reduce number of devices, reduce the volume of whole production technique, simplify the operation, reduce the cost.
Seeing also Fig. 4, is the floor map that the utility model the second embodiment discloses the electroplating solution of cyclic filtering system architecture again.The system 4 of electroplating solution of cyclic filtering shown in the present embodiment is with difference between the upper electroplating solution of cyclic filtering system 3: be connected in series two adjacent plating tanks 41 between the described input channel 413, serial connection two adjacent plating tanks 41 between the described output channel 415.That is to say, when plating bath when described plating tank 41 transfers to described filter vat 43, the plating bath in the different plating tanks 41 is at first after described output channel 413 outputs, via transferring in the described filter vat 43 after unified gathering again.When plating bath when described filter vat 43 transfers to described plating tank 42, plating bath inputs in the corresponding plating tank 41 at the input channel 413 through different plating tanks 41 respectively at first after the output of described filter vat.
In the electroplating solution of cyclic filtering system 4 of present embodiment, described input channel 413 and output channel 415 mutually serial connection arrange, realize the indirect perforation of described plating tank 41 and described filter vat 43, guarantee the abundant mixing of plating bath, the bath parameters of different plating tanks 41 is more consistent, thereby guarantee that more effectively the plating piece product performance after the different plating tank 41 interior plating are consistent, improve production reliability.
Only be better case study on implementation of the present utility model below, be not limited to the utility model, for a person skilled in the art, the utility model can have various modifications and variations.All within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.
Claims (10)
1. electroplating solution of cyclic filtering system, it comprises:
The plating tank of a plurality of tool input channels and output channel;
A plurality of filter pumps that are circulated throughout, and
Filter vat, it is characterized in that: described filter vat and a plurality of plating tank connect mutually by described input channel and output channel, and the described filter pump that is circulated throughout is controlled described electroplate liquid and circulated between described a plurality of plating tanks, described input channel, described output channel and described filter vat.
2. electroplating solution of cyclic filtering according to claim 1 system, it is characterized in that: input channel one end of described plating tank and described plating tank internal run-through, the other end and described filter vat connect with each other.
3. electroplating solution of cyclic filtering according to claim 2 system, it is characterized in that: described output channel one end and described plating tank internal run-through, the other end and described filter vat connect with each other.
4. electroplating solution of cyclic filtering according to claim 3 system, it is characterized in that: the input channel of adjacent plating tank and output channel are connected in series setting mutually.
5. according to claim 2 or 3 described electroplating solution of cyclic filtering systems, it is characterized in that: the described filter pump that is circulated throughout comprises that first is circulated throughout filter pump and second and is circulated throughout filter pump, described first is circulated throughout filter pump closes on the setting of described input channel side, and described second is circulated throughout filter pump closes on the setting of described output channel side.
6. electroplating solution of cyclic filtering according to claim 5 system is characterized in that: described electroplating solution of cyclic filtering system also comprises the cycle control module, and described cycle control module is circulated throughout the corresponding electrical connection of filter pump and arranges with described.
7. electroplating solution of cyclic filtering according to claim 6 system, it is characterized in that: described cycle control module produces the first control signal and controls described the first circulating filtration pump work, and described first is circulated throughout filter pump orders about electroplate liquid and be circulated to described filter vat from described plating tank.
8. electroplating solution of cyclic filtering according to claim 7 system, it is characterized in that: described cycle control module produces the second control signal and controls described the second circulating filtration pump work, and described second is circulated throughout filter pump orders about electroplate liquid and be circulated to described plating tank from described filter vat.
9. electroplating solution of cyclic filtering according to claim 1 system, it is characterized in that: described filter vat is folded between the described plating tank.
10. electroplating solution of cyclic filtering according to claim 1 system, it is characterized in that: described input channel and described output channel are to adopt plastic cement material to process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220397326 CN202830213U (en) | 2012-08-10 | 2012-08-10 | Plating solution circulation filtration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220397326 CN202830213U (en) | 2012-08-10 | 2012-08-10 | Plating solution circulation filtration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202830213U true CN202830213U (en) | 2013-03-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220397326 Expired - Lifetime CN202830213U (en) | 2012-08-10 | 2012-08-10 | Plating solution circulation filtration system |
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| Country | Link |
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| CN (1) | CN202830213U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102851728A (en) * | 2012-08-10 | 2013-01-02 | 梅州市志浩电子科技有限公司 | System and method for plating solution circulating filtration |
-
2012
- 2012-08-10 CN CN 201220397326 patent/CN202830213U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102851728A (en) * | 2012-08-10 | 2013-01-02 | 梅州市志浩电子科技有限公司 | System and method for plating solution circulating filtration |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130327 |
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| CX01 | Expiry of patent term |