CN201416042Y - Electroplating tank - Google Patents
Electroplating tank Download PDFInfo
- Publication number
- CN201416042Y CN201416042Y CN2009201855393U CN200920185539U CN201416042Y CN 201416042 Y CN201416042 Y CN 201416042Y CN 2009201855393 U CN2009201855393 U CN 2009201855393U CN 200920185539 U CN200920185539 U CN 200920185539U CN 201416042 Y CN201416042 Y CN 201416042Y
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- electroforming
- purifying area
- workspace
- overflow
- solution
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Abstract
The utility model relates to an electroplating device for covering a metal layer on the surface of fine mould, and particularly to an electroplating tank. The electroplating tank comprises a housing and three continuous areas provided in the housing. The areas are respectively an electroplating purifying area, an electroplating operating area and an overflow purifying area. The electroforming purifying area is provided with an electric metal impurity removing device, a heating device and an electroplating drug adding device. The electroplating operating area is provided with an electroplatinganode, an electroplating cathode and an electroplating solution mixer. The overflow purifying area is provided with an electroplating solution level detector and a supply device. The electroplating device provided by the utility model realizes the purification of electroplating solution in continuous production, settles the problem that the electroplating solution is polluted, reduces the shutdowntime and increases the production efficiency. The surface smoothness and flatness of the electroplating master mould are greatly increased. No peculiar smell exists in the electroplating plate, and the working environment is improved greatly.
Description
Technical field
The utility model relates to a kind of electroforming apparatus at precision die surface coverage metal level, specifically relates to the electrotyping bath in this kind equipment.
Background technology
The application of electroforming in industry day by day deeply, main as producing various being difficult to machining process manufacturing or the very high part of tooling cost, many important application have been obtained in fields such as precision die, aerospace, weapons manufacturings, as optical precision mould, rocket combustion chamber, edm electrode, receiving set telerecording indicator, laser anti-counterfeit trade mark masterplate etc.
This class electoformed product has very high accuracy requirement usually, and needs certain thickness requirement, as: the optics die of using as the Reflex Reflector injection mold just needs general 15mm thickness.Yet for the high electoformed product of accuracy requirement, the electroformed layer that forms 1mm just needs 24 hours electroforming time, therefore as forming the electroformed layer of 20mm thickness, just need 20 days electroforming time.In this very long depositing time, must guarantee that electroforming solution keeps the stable of pure and processing parameter (additive level, temperature, liquid level etc.), if just electroforming reprocessing again of mistake is arranged slightly, thereby influence efficient more.
Existing electrotyping bath has only an electroforming workspace, electroforming solution purifies, adds, heats and all finish in this workspace, be difficult to guarantee that electroforming solution keeps the stable of pure and processing parameter (additive level, temperature, liquid level etc.), the electroforming poor effect, the electroforming success ratio is not high, and electroforming master mold surface smoothness and planeness are not fine.
Summary of the invention
Therefore; the purpose of this utility model is to provide a kind of novel high-efficiency and continuous to purify electrotyping bath, has realized keeping the pure while of electroforming solution can stablize the processing parameter of electroforming in continuous production, has solved the contaminated problem of electroforming solution in the production; reduce stop time, enhance productivity.
In order to realize the utility model purpose, adopt following technical proposals to solve:
A kind of electrotyping bath comprises casing, is located at intravital continuous three zones of casing successively, is respectively electroforming purifying area, electroforming workspace and overflow purifying area.
Be provided with electrolysis in the electroforming purifying area and remove metallic impurity device, heating unit and the import of electroforming medicament adding set; Be provided with electroforming anode, electroforming negative electrode in the electroforming workspace; Be provided with electroforming solution liquid level detection device and supplementary device in the described overflow purifying area.
Be provided with the electroforming solution partitioning device between electroforming purifying area and the electroforming workspace, electroforming solution from the electroforming purifying area by the overflow of electroforming solution partitioning device to the electroforming workspace, be provided with between electroforming workspace and the electroforming purifying area and make the reflux that electroforming solution can be from the engine housing external reflux to the electroforming purifying area; Be provided with electroforming solution subregion equipment between electroforming workspace and the overflow purifying area, electroforming solution from the electroforming workspace by the overflow of electroforming solution subregion equipment to the overflow purifying area, be provided with between overflow purifying area and the electroforming purifying area and make the refluxing unit that electroforming solution can be from the engine housing external reflux to the electroforming purifying area.
Technique scheme also can be done further perfect by following change:
Because heating unit and medicament added automatically system are located in the electroforming purifying area, the volume of described electroforming purifying area splendid attire electroforming solution is greater than the volume of electroforming workspace splendid attire electroforming solution, and generally be controlled between 1.5 to 5 times, more excellent with about 2 times, this design guarantees the stable of electroforming solution processing parameter (additive level, temperature etc.) and meets in electroforming workspace processing requirement, has guaranteed that electroforming is stable.Because the electroforming solution total volume of electroforming purifying area is an electroforming workspace more than 1.5 times, electroforming solution removes through electrolysis at the electroforming purifying area that metallic impurity purify simultaneously, overflow enters the electroforming workspace after the temperature control system heating, medicament added automatically system, and uniflux.Therefore, electroforming solution in the electroforming workspace is reasonably replaced through the highly purified soup of purifying treatment, thereby has guaranteed electroforming solution pure in the electroforming workspace, and has guaranteed the stable of electroforming process parameter (additive level, temperature etc.).On the other hand, recycling of electroforming solution need not replenish the described electroforming system that obtains by the external world, thereby when ensureing the electroforming process parameter stability, can greatly reduce maintenance cost.
And the volume of electroforming workspace splendid attire electroforming solution also generally is controlled between 2 to 7 times greater than the volume of overflow purifying area splendid attire electroforming solution, and is more excellent with 4 times.The pure water of in the overflow purifying area, adding, through just entering the fluctuation that the electroforming workspace has reduced processing parameter to greatest extent behind the secondary buffer (flow through overflow purifying area and electroforming purifying area), guaranteed the stable of electroforming solution technological work parameter, for precise electrotyping provides sound assurance, reduced production cost.Overflow purifying area electroforming solution derives from the overflow of electroforming workspace, the activated carbon filtration system is set in the district eliminates the pollution of macromole organic impurity, purifies electroforming solution.
The smell is awful owing to electroforming solution, in order to guarantee the working space environment, described chassis sidewall is designed to sandwich structure, is provided with inlet mouth at the chassis sidewall internal layer that is higher than the electroforming solution liquid level, and the chassis sidewall skin is provided with the air outlet, and smell can be concentrated discharging like this.
Described electrolysis removes the metallic impurity device and comprises removal of impurity anode and removal of impurity negative electrode, metals such as the nickel cobalt of electroforming add at anode, described removal of impurity negative electrode is a metallic sieve, screen cloth is inserted in the electroforming purifying area across casing, electroforming solution is passed from screen cloth, mesh size is at 2-7mm, and is made into corrugated, in order to increase electrolytic surface-area.Sieve surface area is greater than removal of impurity anode surface area, the surface area ratio of removal of impurity anode and screen cloth was less than 1: 6, removal of impurity cathode current density is about 0.1 to 0.2 ampere/square decimeter, when electroforming solution flows through from screen cloth, through the low current density electrolytic cleaning, remove impurity metal ions such as cupric ion, zine ion, screen cloth is in case stop up and can change at any time.
Partitioning device between described electroforming purifying area and the electroforming workspace is two interceptors, two interceptors from, the first interceptor two sides near the electroforming purifying area are connected with the chassis sidewall internal layer, bottom surface and casing bottom surface from so that electroforming solution pass through from first interceptor bottom, the second interceptor two sides near the electroforming workspace are connected with the chassis sidewall internal layer, the bottom surface is connected with the casing bottom surface, and electroforming solution enters the electroforming workspace from the second interceptor end face overflow.Micro-bubble is in above the electroforming solution of electroforming workspace always like this, has avoided micro-bubble to enter electroforming solution inside and has been adsorbed on the electroforming master mold and forms pore.
Be provided with the electric current baffle plate between inherent electroforming anode of described electroforming workspace and the electroforming negative electrode, perforate on the electric current baffle plate, the size in hole is consistent with the electroforming area of electroforming master mold on being installed in the electroforming negative electrode, and with the parallel installation of electroforming master mold.This electric current baffle plate simulation pictograph anodic design makes the current density of whole electroforming master mold in the electroforming work even to greatest extent, has reduced the phenomenon of streaming of electric current, has guaranteed the electoformed product steady quality.
Subregion equipment between described electroforming workspace and the overflow purifying area comprises the subregion baffle plate, and subregion baffle plate two sides are connected with the chassis sidewall internal layer, and the bottom surface is connected with the casing bottom surface, electroforming solution from the overflow of subregion baffle plate end face to the overflow purifying area.Macromole organic impurity in the electroforming soup can be suspended in the surface of the electroforming solution of overflow purifying area, the electroforming solution that contains the larger molecular organics floating matter is like this collected through overflow, by active carbon filtering device, remove the macromole organic impurity to ensure carrying out smoothly of precise electrotyping work.It is the microfroc filter of 1 μ m that filtration unit adopts the maximum filtering aperture, and dress adsorbs the macromole organic impurity as granular gac in filter.Its filtration yield hourly is more than five times of overflow purifying area electroforming solution total amount, to guarantee the pure of electroforming solution, reduces the macromole organic impurity influence in the electroforming solution.Overflow enters the electroforming solution of overflow purifying area, enters the electrolytic cleaning district through behind the activated carbon filtration.
Described electroforming solution liquid level detection device and supplementary device are float(ing)valve.In case when the electroforming solution liquid level was lower than design, the float(ing)valve action can obtain pure water and replenish in the overflow purifying area.
Electroforming solution in the described electroforming workspace comprises return line from engine housing external reflux to the reflux that the electroforming purifying area is adopted, the return line import is positioned at electroforming workspace bottom, the return line outlet is between the removal of impurity anode and removal of impurity negative electrode of electroforming purifying area, and the electroforming solution after the backflow can be purified again.Return line is provided with accurate filter, this accurate filter is a prior art, it is the accurate filter of 1 μ m that filtration unit adopts the maximum filtering aperture, accurate filter filtration yield hourly is more than ten times of electroforming workspace electroforming solution total amount, to guarantee the pure of electroforming solution, reduce the influence of granule foreign in the electroforming solution.
Electroforming solution in the described overflow purifying area comprises return line from engine housing external reflux to the refluxing unit that the electroforming purifying area is adopted, the return line import is positioned at overflow purifying area bottom, the return line outlet is between the removal of impurity anode and removal of impurity negative electrode of electroforming purifying area, and the electroforming solution after the backflow can be purified again.Described return line is provided with the gac device of absorption larger molecular organics.
By technique scheme, can draw and the utlity model has following advantage: this patent has been realized keeping the pure of electroforming solution in continuous production, has solved the contaminated problem of electroforming solution in the production, reduces stop time, enhances productivity.Electroforming master mold surface smoothness and smoothness are all improved greatly, electroforming place air free from extraneous odour, Working environment improves greatly.
Description of drawings
Fig. 1 is the embodiment stereographic map;
Fig. 2 is another angle stereographic map of embodiment;
Fig. 3 dissects a part of product stereographic map in back for embodiment;
Fig. 4 is another part product stereographic map of embodiment after dissecing;
Fig. 5 is the embodiment vertical view.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
Embodiment, in conjunction with Fig. 1 to Fig. 5, a kind of electrotyping bath, comprise casing 1, be located at intravital continuous three zones of casing, be respectively electroforming purifying area 2, electroforming workspace 3 and overflow purifying area 4, the electroforming solution volume of electroforming purifying area 2 dresses is 2 times of electroforming workspace 3, and the electroforming solution volume of overflow purifying area 4 dresses is 20% of an electroforming workspace 3.Casing 1 sidewall is a sandwich structure, and the chassis sidewall internal layer that is higher than the electroforming solution liquid level is provided with inlet mouth 11, and the chassis sidewall skin is provided with air outlet 12, and the air outlet connects with the extraneous gas barrier (not shown) that is connected, and realizes concentrating the discharging of bleeding.
Initial end is provided with removal of impurity anode 20 and removal of impurity negative electrode 21 in the electroforming purifying area 2, and described removal of impurity negative electrode 21 is a stainless steel mesh, and screen cloth is inserted in the electroforming purifying area across casing 1, and sieve surface area is greater than removal of impurity anode surface area.Also be provided with the electric heating tube 22 and the electroforming medicament adding set 23 of heating usefulness in the electroforming purifying area, for example controlling the electroforming solution temperature automatically is 50 ± 1 ℃, automatically regulating hydrogen ion concentration is 4.1 ± 0.1pH, suitably regulates the deposition stress of electroforming solution automatically by the control adding of additive.In case electroforming medicament adding set detects hydrogen ion concentration or deposition stress departs from set(ting)value, electroforming medicament adding set is opened the electroforming medicament and is added electroforming purifying area 2, present embodiment only shows the import of electroforming medicament adding set in the drawings, and this device is the prior art Therefore, omited.
Be provided with two interceptors 24,30 between electroforming purifying area 2 and the electroforming workspace 3, two interceptors from, first interceptor, 24 two sides are connected with casing 1 side wall inner layer, bottom surface and casing bottom surface from so that electroforming solution pass through from first interceptor, 24 bottoms, second interceptor, 30 two sides are connected with the chassis sidewall internal layer, the bottom surface is connected with the casing bottom surface, and electroforming solution enters electroforming workspace 3 from the 30 end face overflows of second interceptor.
Be provided with electroforming anode 31, electric current baffle plate 32, electroforming negative electrode 33 in the electroforming workspace 3.The electroforming master mold is an electroforming negative electrode 33.Be provided with electric current baffle plate 32 (being used to simulate the pictograph anode working) between electroforming anode 31 and the electroforming negative electrode 33, perforate 34 on the electric current baffle plate 32, and the size in hole 34 is consistent with the electroforming area of electroforming master mold on being installed in the electroforming negative electrode.
Be provided with between electroforming workspace 3 and the electroforming purifying area 2 and make the reflux that electroforming solution can be from the engine housing external reflux to the electroforming purifying area.Described reflux comprises return line 5A and return line 5B, and return line 5A and return line 5B import are positioned at electroforming workspace 3 bottoms, return line 5A and return line 5B outlet electroforming purifying area 2 between removal of impurity anode 20 and removal of impurity negative electrode 21.Described return line is provided with the accurate filter (not shown), and every accurate filter filtration yield hourly is more than ten times of electroforming workspace electroforming solution total amount, to guarantee the pure of electroforming solution, reduces the influence of granule foreign in the electroforming solution.Accelerate the uniflux of electroforming solution simultaneously, play the intensive mixing effect, in time replenish the ionic concn on electroformed layer surface.Compare with traditional stirring means (as gas stirring) have the efficient height, the advantages such as (as koniology etc.) of can not introducing new source of pollution from the external world, reduce electroforming process fluctuation (causing the temperature fluctuation of electroforming solution as pneumatic blending), improved the accuracy of electroforming.
Be provided with subregion baffle plate 40 between electroforming workspace 3 and the overflow purifying area 4, subregion baffle plate 40 two sides are connected with the chassis sidewall internal layer, and the bottom surface is connected with the casing bottom surface, electroforming solution from the overflow of subregion baffle plate end face to the overflow purifying area.
Be provided with the float(ing)valve 41 that detects electroforming solution liquid level and additional pure water in the described overflow purifying area 4.
Be provided with between overflow purifying area 4 and the electroforming purifying area 2 and make the refluxing unit that electroforming solution can be from the engine housing external reflux to the electroforming purifying area.Described refluxing unit comprises return line 6, and return line 6 imports are positioned at overflow purifying area 4 bottoms, and return line 6 outlets are between the removal of impurity anode 20 and removal of impurity negative electrode 21 of electroforming purifying area.Described return line 6 is provided with the adsorber (not shown) of absorption larger molecular organics.
Although below in conjunction with specific embodiments the utility model is described in detail, the utility model should not be confined to above-mentioned specific embodiment or scheme.Under the prerequisite that does not exceed spirit and scope of the present utility model, those of ordinary skills can make amendment to the above embodiments, technical scheme or technical characterictic combination.
Claims (10)
1, a kind of electrotyping bath, comprise casing, be located at the intravital electroforming workspace of casing, be provided with the electroforming anode in the electroforming workspace, the electroforming negative electrode, it is characterized in that: also be provided with electroforming purifying area and overflow purifying area in the described engine housing, electroforming purifying area and overflow purifying area lay respectively at electroforming workspace two ends, be provided with electrolysis in the electroforming purifying area and remove the metallic impurity device, heating unit and the import of electroforming medicament adding set, be provided with the electroforming solution partitioning device between electroforming purifying area and the electroforming workspace, electroforming solution is passed through the overflow of electroforming solution partitioning device to the electroforming workspace from the electroforming purifying area, be provided with between electroforming workspace and the electroforming purifying area and make the reflux that electroforming solution can be from the engine housing external reflux to the electroforming purifying area, be provided with electroforming solution liquid level detection device and supplementary device in the described overflow purifying area, be provided with electroforming solution subregion equipment between electroforming workspace and the overflow purifying area, electroforming solution from the electroforming workspace by the overflow of electroforming solution subregion equipment to the overflow purifying area, be provided with between overflow purifying area and the electroforming purifying area and make the refluxing unit that electroforming solution can be from the engine housing external reflux to the electroforming purifying area.
2, according to the described electrotyping bath of claim 1, it is characterized in that: described electroforming purifying area volume is 1.5 to 5 times of electroforming workspace volumetrical, and electroforming workspace volume is 2 to 7 times of overflow purifying area volumetrical.
3, according to claim 1 or 2 described electrotyping baths, it is characterized in that: described chassis sidewall is a sandwich structure, and the chassis sidewall internal layer that is higher than the electroforming solution liquid level is provided with inlet mouth, and the chassis sidewall skin is provided with the air outlet.
4, according to the described electrotyping bath of claim 1, it is characterized in that: described electrolysis removes the metallic impurity device and comprises removal of impurity anode and removal of impurity negative electrode, described removal of impurity negative electrode is a metallic sieve, and screen cloth is inserted in the electroforming purifying area across casing, and sieve surface area is greater than removal of impurity anode surface area.
5, according to the described electrotyping bath of claim 1, it is characterized in that: described partitioning device comprises two interceptors, two interceptors from, the first interceptor two sides near the electroforming purifying area are connected with the chassis sidewall internal layer, bottom surface and casing bottom surface from so that electroforming solution pass through from first interceptor bottom, the second interceptor two sides near the electroforming workspace are connected with the chassis sidewall internal layer, and the bottom surface is connected with the casing bottom surface, and electroforming solution enters the electroforming workspace from the second interceptor end face overflow.
6, according to the described electrotyping bath of claim 1, it is characterized in that: be provided with the electric current baffle plate between inherent electroforming anode of described electroforming workspace and the electroforming negative electrode, perforate on the electric current baffle plate, the size in hole is consistent with the electroforming area of electroforming master mold on being installed in the electroforming negative electrode.
7, according to the described electrotyping bath of claim 1, it is characterized in that: described subregion equipment comprises the subregion baffle plate, and subregion baffle plate two sides are connected with the chassis sidewall internal layer, and the bottom surface is connected with the casing bottom surface, electroforming solution from the overflow of subregion baffle plate end face to the overflow purifying area.
8, according to the described electrotyping bath of claim 1, it is characterized in that: electroforming solution liquid level detection device and supplementary device are float(ing)valve.
9, according to the described electrotyping bath of claim 4, it is characterized in that: described reflux comprises return line, the return line import is positioned at electroforming workspace bottom, and return line exports between the removal of impurity anode and removal of impurity negative electrode of electroforming purifying area, and return line is provided with accurate filter.
10, according to the described electrotyping bath of claim 4, it is characterized in that: described refluxing unit comprises return line, the return line import is positioned at overflow purifying area bottom, the return line outlet is between the removal of impurity anode and removal of impurity negative electrode of electroforming purifying area, and described return line is provided with the adsorber of absorption larger molecular organics.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201855393U CN201416042Y (en) | 2009-06-17 | 2009-06-17 | Electroplating tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201855393U CN201416042Y (en) | 2009-06-17 | 2009-06-17 | Electroplating tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201416042Y true CN201416042Y (en) | 2010-03-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009201855393U Expired - Fee Related CN201416042Y (en) | 2009-06-17 | 2009-06-17 | Electroplating tank |
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| CN (1) | CN201416042Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103205784A (en) * | 2012-01-16 | 2013-07-17 | 昆山允升吉光电科技有限公司 | A preparation method for a vapor plating mask plate |
| CN103205782A (en) * | 2012-01-16 | 2013-07-17 | 昆山允升吉光电科技有限公司 | A preparation method for a vapor plating mask plate made from a nickel-iron alloy |
| CN103205714A (en) * | 2012-01-16 | 2013-07-17 | 昆山允升吉光电科技有限公司 | A metal mask for vapor plating and a production method thereof |
| CN104372385A (en) * | 2013-08-13 | 2015-02-25 | 赛特莱特（佛山）塑胶制品有限公司 | Electroforming tank |
-
2009
- 2009-06-17 CN CN2009201855393U patent/CN201416042Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103205784A (en) * | 2012-01-16 | 2013-07-17 | 昆山允升吉光电科技有限公司 | A preparation method for a vapor plating mask plate |
| CN103205782A (en) * | 2012-01-16 | 2013-07-17 | 昆山允升吉光电科技有限公司 | A preparation method for a vapor plating mask plate made from a nickel-iron alloy |
| CN103205714A (en) * | 2012-01-16 | 2013-07-17 | 昆山允升吉光电科技有限公司 | A metal mask for vapor plating and a production method thereof |
| CN103205714B (en) * | 2012-01-16 | 2015-06-10 | 昆山允升吉光电科技有限公司 | A metal mask for vapor plating and a production method thereof |
| CN104372385A (en) * | 2013-08-13 | 2015-02-25 | 赛特莱特（佛山）塑胶制品有限公司 | Electroforming tank |
| CN104372385B (en) * | 2013-08-13 | 2016-09-28 | 赛特莱特（佛山）塑胶制品有限公司 | Electrotyping bath |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100303 Termination date: 20110617 |