CN205115659U - Anode system of plating solution separation - Google Patents
Anode system of plating solution separation Download PDFInfo
- Publication number
- CN205115659U CN205115659U CN201520885969.1U CN201520885969U CN205115659U CN 205115659 U CN205115659 U CN 205115659U CN 201520885969 U CN201520885969 U CN 201520885969U CN 205115659 U CN205115659 U CN 205115659U
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- CN
- China
- Prior art keywords
- anode
- electroplate liquid
- anolyte
- separation
- sealing
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
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Abstract
The utility model discloses an anode system of plating solution separation, including plating bath and piece -rate system, the plating solution is equipped with in the plating bath, the piece -rate system submergence is in the plating solution, and the piece -rate system is closed tubular structure in the tubular structure of piece -rate system was located to diaphragm between upper and lower sealing member, anode bar and upper and lower sealing member, anode bar, the diaphragm was porous structure, parts anode bar and plating solution, realizes plating solution and anode liquor ion exchange. Furtherly still includes anode liquor accumulator, transmission pipeline, last flowmeter and the force pump of being equipped with of transmission pipeline, and transmission pipeline connects piece -rate system and anode liquor accumulator, realizes anode liquor circulation between anode liquor accumulator and piece -rate system.
Description
Technical field
The utility model relates to the anode system that a kind of electroplate liquid is separated.
Background technology
Cathode sheets and the anode bar of existing galvanic anode system are all established with identical electrolytic solution, a large amount of oxidation of organic compounds is had in electroplating process, nickel in electrolytic solution may produce prussiate, because organic oxidation adds the formation of carbonate, seriously, quantity of heat production is very large, only has about 50%-60% electric current for galvanic deposit for electrolyte contamination and loss, remaining current draw, in heat production and liberation of hydrogen, needs powerful cooling apparatus simultaneously.
Utility model content
The utility model provides to solve deficiency of the prior art the anode system that a kind of electroplate liquid is separated, and deposition current is large, sedimentation rate is fast, and electrolytic solution loss is little, capacity efficiency is high.
For achieving the above object, the technical solution adopted in the utility model is:
The anode system that a kind of electroplate liquid is separated, comprise plating tank and separation system, plating tank is built with electroplate liquid, separation system is immersed in electroplate liquid, and separation system is closed structure, comprises upper and lower sealing member, barrier film between anode bar and upper-lower seal part, anode bar is located in the tubular construction of separation system, barrier film is vesicular structure, anode bar and electroplate liquid is separated, and realizes electroplate liquid and anolyte ions exchange.Anolyte and electroplate liquid separate by barrier film, and the oxide compound that anode produces is transported by anolyte and discharges, and avoids oxide dissolution in electroplate liquid, can prevent the oxidation of organic compound in electroplate liquid.
As a kind of preferred version of the anode system that electroplate liquid described in the utility model is separated, described separation system comprises sealing member, lower seal, the barrier film of both ends open, hold-down bars, anode bar with sealing cover, the upper surface of upper sealing member lower surface and lower seal is provided with sealing groove, sealing-ring is provided with in sealing groove, upper sealing member and lower seal outer are provided with several fixed orificess in one week, and fixed orifices is arranged on the outside of sealing groove.
As a kind of preferred version of the anode system that electroplate liquid described in the utility model is separated, described upper sealing member has upper and lower opening and a side opening, upper and lower opening forms a passage, this passage is communicated with barrier film, side opening and above-mentioned channel connection, anode bar upper end is fixed with circular seal lid, anode bar runs through sealing cover and closely fixes, also liquid-inlet pipe is provided with along anode bar, liquid-inlet pipe upper end is fixed on sealing cover, liquid-inlet pipe lower end and anode bar lower end are fixed, and liquid-inlet pipe is used for anolyte to introduce bottom separation system.Further, liquid-inlet pipe end is located at the bottom surface position in separation system, the anolyte newly supplemented into can be allowed fully to react, circulate more thorough.
As a kind of preferred version of the anode system that electroplate liquid described in the utility model is separated, also comprise anolyte accumulator tank, transfer conduit, transfer conduit is provided with under meter and pressure pump, separation system is connected with anolyte accumulator tank by transfer conduit, realizes anolyte and is circulating between anolyte accumulator tank and separation system.Can realizing automatically supplementing of anolyte, simultaneously by regulating the anode electrolysis flow velocity of the under meter in transfer conduit, regulating the pressure in separation system, and then control the exchange velocity of ion by barrier film, be that whole system is stable.
As a kind of preferred version of the anode system that electroplate liquid described in the utility model is separated, comprise multiple separation system in a described anode system, different separation systems is arranged in same plating tank by the demand of physical device.
As a kind of preferred version of the anode system that electroplate liquid described in the utility model is separated, described barrier film is mineral membrane or organic membrane, and as being porous ceramic film, do not need extra bracing frame to support, structure is simple.
As a kind of preferred version of the anode system that electroplate liquid described in the utility model is separated, in described anolyte accumulator tank, be provided with agitator.
Accompanying drawing explanation
Fig. 1 is the anode system structural representation that described electroplate liquid is separated.
Wherein:
1, plating tank 2, separation system 3, anolyte accumulator tank 4, transfer conduit 5, under meter 6, pressure pump
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Embodiment 1
The anode system that a kind of electroplate liquid is separated, plating tank 1, several separation systems 2, anolyte accumulator tank 3, transfer conduit 4, transfer conduit is provided with under meter 5 and pressure pump 6, separation system 2 is connected with anolyte accumulator tank 3 by transfer conduit 4, realize anolyte circulating between anolyte accumulator tank and separation system, plating tank is built with electroplate liquid, and separation system is placed by demand and is immersed in electroplate liquid.
Wherein separation system is closed structure, comprise sealing member, lower seal, the barrier film of both ends open, hold-down bars, anode bar with sealing cover, the upper surface of upper sealing member lower surface and lower seal is provided with sealing groove, sealing-ring is provided with in sealing groove, upper sealing member and lower seal outer are provided with several fixed orificess in one week, and fixed orifices is arranged on the outside of sealing groove.Hold-down bars is fixed between sealing member and lower seal, for supporting and restriction above sealing member and lower seal.Upper sealing member has upper and lower opening and a side opening, and upper and lower opening forms a passage, and this passage is communicated with barrier film, and side opening and above-mentioned channel connection, the upper shed of upper sealing member has outside screw.Side opening is used for the anolyte in separation system to discharge.Anode bar upper end is fixed with circular seal lid, anode bar runs through sealing cover and closely fixes, and be also provided with liquid-inlet pipe along anode bar, liquid-inlet pipe upper end is fixed on sealing cover, liquid-inlet pipe lower end and anode bar lower end are fixed, and liquid-inlet pipe is used for anolyte to introduce bottom separation system.Barrier film is vesicular structure, anode bar and electroplate liquid is separated, and realizes electroplate liquid and anolyte ions exchange.Further, barrier film arranges and can be organic membrane and mineral membrane, does not need extra bracing frame to support, and structure is simple, is easy to produce.
During installation, first sealing-ring is fit in sealing groove, then the fixed orifices of lower seal inserted in the lower end of hold-down bars and fix with nut, then by the lower end of barrier film insert lower seal sealing groove in and press seal circle, sealing-ring is loaded by the sealing groove of upper sealing member, then sealing groove and fixed orifices are aimed at barrier film and fixed orifices respectively, then with bolt, upper sealing member and hold-down bars are fixed.After fixing sealing member, anode bar with liquid-inlet pipe is inserted in separation system, the sealing cover of anode bar upper end and the inwall of upper sealing member compress, in order to improve sealing effectiveness, at sealing cover and the inwall of upper sealing member, sealing-ring is set, finally screw with the female fixed cap of band and upper sealing member, complete the installation of a separation system.
Anode bar above in embodiment is a sheet structure, but as required, and anode bar also can be made into cylindric or with the arc-shaped of different angles.Anode bar can be titanium iridium alloy, nickelalloy, stainless steel etc.Anolyte accumulator tank is made up of alkali resistant materials, as being polypropylene.In order to eliminate the gas produced in anode, an agitator can be added in electrolytic solution accumulator tank.
Said apparatus Anodic electrolytic solution comprises sodium hydroxide, silicate, zine ion, nickel ion and water, and electroplate liquid is basic solution, can be applied to zinc and Zinc alloy electroplating industry, as zinc-iron, zinc cobalt, zinc-nickel, zinc-tin electroplating solution.
Although be illustrated embodiment of the present utility model in specification sheets, these embodiments just as prompting, should not limit protection domain of the present utility model.In the scope not departing from the utility model aim, carry out various omission, displacement and change all should be included in protection domain of the present utility model.
Claims (9)
1. the anode system of an electroplate liquid separation, comprise plating tank and separation system, plating tank is built with electroplate liquid, separation system is immersed in electroplate liquid, it is characterized in that: separation system is closed structure, comprises upper and lower sealing cover, barrier film between anode bar and upper-lower seal part, anode bar is located in the tubular construction of separation system, barrier film is vesicular structure, anode bar and electroplate liquid is separated, and realizes electroplate liquid and anolyte ions exchange.
2. the anode system of electroplate liquid separation according to claim 1, it is characterized in that: described separation system comprises sealing member, lower seal, the tubular barrier film of both ends open, hold-down bars, anode bar with sealing cover, the upper surface of upper sealing member lower surface and lower seal is provided with sealing groove, sealing-ring is provided with in sealing groove, upper sealing member and lower seal outer are provided with several fixed orificess in one week, and fixed orifices is arranged on the outside of sealing groove.
3. the anode system of electroplate liquid separation according to claim 2, it is characterized in that: described upper sealing member has upper and lower opening and a side opening, upper and lower opening forms a passage, this passage is communicated with barrier film, side opening and above-mentioned channel connection, anode bar upper end is fixed with circular seal lid, anode bar runs through sealing cover and closely fixes, also liquid-inlet pipe is provided with along anode bar, liquid-inlet pipe upper end is fixed on sealing cover, liquid-inlet pipe lower end and anode bar lower end are fixed, and liquid-inlet pipe is used for anolyte to introduce bottom separation system.
4. the anode system of electroplate liquid separation according to claim 3, it is characterized in that: also comprise anolyte accumulator tank, transfer conduit, transfer conduit is provided with under meter and pressure pump, separation system is connected with anolyte accumulator tank by transfer conduit, realizes anolyte and is circulating between anolyte accumulator tank and separation system.
5. the anode system of electroplate liquid separation according to claim 1, is characterized in that: described electroplate liquid is basic solution.
6. the anode system of electroplate liquid separation according to claim 5, is characterized in that: described electroplate liquid is zinc and Zinc alloy electroplating liquid.
7. the anode system that is separated of electroplate liquid according to claim 1, is characterized in that: comprise multiple separation system in a described anode system, different separation systems according to actual demand can in various degree and be listed in same plating tank.
8. the anode system of electroplate liquid separation according to claim 3, is characterized in that: described barrier film is mineral membrane or organic membrane.
9. the anode system of electroplate liquid separation according to claim 4, is characterized in that: be provided with agitator in described anolyte accumulator tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520885969.1U CN205115659U (en) | 2015-11-09 | 2015-11-09 | Anode system of plating solution separation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520885969.1U CN205115659U (en) | 2015-11-09 | 2015-11-09 | Anode system of plating solution separation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205115659U true CN205115659U (en) | 2016-03-30 |
Family
ID=55571281
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520885969.1U Withdrawn - After Issue CN205115659U (en) | 2015-11-09 | 2015-11-09 | Anode system of plating solution separation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205115659U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105350063A (en) * | 2015-11-09 | 2016-02-24 | 科文特亚表面处理技术（苏州）有限公司 | Electroplating-liquid-separated anode system |
-
2015
- 2015-11-09 CN CN201520885969.1U patent/CN205115659U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105350063A (en) * | 2015-11-09 | 2016-02-24 | 科文特亚表面处理技术（苏州）有限公司 | Electroplating-liquid-separated anode system |
| CN105350063B (en) * | 2015-11-09 | 2018-10-30 | 科文特亚环保电镀技术（江苏）有限公司 | A kind of anode system of electroplate liquid separation |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160330 Effective date of abandoning: 20181030 |