CN204080160U - A kind of alkaline zinc plating electrolytic plating pool - Google Patents
A kind of alkaline zinc plating electrolytic plating pool Download PDFInfo
- Publication number
- CN204080160U CN204080160U CN201420371040.2U CN201420371040U CN204080160U CN 204080160 U CN204080160 U CN 204080160U CN 201420371040 U CN201420371040 U CN 201420371040U CN 204080160 U CN204080160 U CN 204080160U
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- CN
- China
- Prior art keywords
- plating
- zinc
- hanging basket
- insoluble
- groove
- Prior art date
- 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.)
- Expired - Lifetime
Links
- 238000007747 plating Methods 0.000 title claims abstract description 55
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title claims abstract description 47
- 229910052725 zinc Inorganic materials 0.000 title claims abstract description 47
- 239000011701 zinc Substances 0.000 title claims abstract description 47
- 238000009713 electroplating Methods 0.000 title claims abstract description 25
- 230000002093 peripheral effect Effects 0.000 claims abstract description 7
- 239000000243 solution Substances 0.000 claims description 19
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 18
- 229910052742 iron Inorganic materials 0.000 claims description 9
- 239000008151 electrolyte solution Substances 0.000 claims description 5
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 abstract description 5
- 239000011248 coating agent Substances 0.000 description 15
- 238000000576 coating method Methods 0.000 description 15
- 238000005260 corrosion Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000005246 galvanizing Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000002161 passivation Methods 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Electroplating And Plating Baths Therefor (AREA)
Abstract
The utility model relates to a kind of alkaline zinc plating electrolytic plating pool, described electrolytic plating pool comprises plating tank, positive plate and connecting pipe, described plating tank comprises plating major trough and molten zinc groove, plating major trough is communicated with by filter with molten zinc groove, positive plate is arranged on plating major trough inwall both sides and positive plate is insoluble anode, arrange a telescopic bar directly over molten zinc groove, telescopic bar bottom arranges an insoluble hanging basket, gives insoluble hanging basket peripheral hardware one energized equipment simultaneously.The utility model has the advantage of: the utility model by regulate the height of telescopic bar by control to immerse zinc ball in solution number, the height of zinc ion concentration in plating solution can be controlled flexibly, ensure the stable of plating solution, and it is simple to operate laborsaving, substantially increase the stability of quality product, and reduce labour intensity.
Description
Technical field
The utility model relates to a kind of electrolytic plating pool, especially a kind of alkaline zinc plating electrolytic plating pool.
Background technology
Electro-galvanizing is also named cold galvanizing, that workpiece is placed in electrolytic solution, that plated metal is separated out and is deposited on workpiece and forms coating, its coating is pot galvanize ratio comparatively, thinner, be generally 4-12 micron, the quality of coating is most important link, due to speed in the process of plating, distribution of current is uneven, the factor such as the dispersive ability of electroplating solution is not strong, the thickness of coating at a goods position can be caused uneven, and the corrosion resistance of coating depends primarily on thickness of coating and exposed environments, the coating that working conditions more badly needs is thicker, and the corrosion resistance of whole coating depends on that the weakest part of coating comprises the resistance to corrosion in the minimum place of local thickness, general present situation, thickness coating is added in order to obtain better solidity to corrosion, undoubtedly in the waste adding cost and zinc metal, and coating is thicker, the internal stress of coating is larger, coating easily comes off, also easily produce coarse, the flaw such as to burn, and the place that coating is excessively thin, low in glossiness, obfuscation, send out mist, easily show-through in the process of bright dipping and passivation.No matter from non-corrosibility, or outward appearance, the aspects such as machinability, all wish the homogeneity of the thickness improving product each position coating, reduce extreme difference.
The zinc-plated direct employing zine plate of conventional alkaline is as anode, and when anode quantity is very few, easy passivation is not dissolved, when anode quantity is too much, zinc concentration to be caused in solution to raise, and after anode dissolution shortens, can affect conductivity, these all can affect the stability of plating solution, and then affect quality product.Therefore just must develop a kind of electrolytic plating pool that can control zinc ion concentration height in plating solution flexibly, not find the same or analogous device with the utility model through retrieval.
Summary of the invention
The technical problems to be solved in the utility model is to provide a kind of electrolytic plating pool that can control zinc ion concentration height in plating solution flexibly.
For solving the problems of the technologies described above, the technical solution of the utility model is: a kind of alkaline zinc plating electrolytic plating pool, comprise a plating tank, electroplating solution is had in plating tank, and one piece is arranged on plating tank inwall upper anode plate, also comprise peripheral hardware direct supply and a plating piece, direct supply forms loop line by wire and positive plate, plating piece, electroplating solution, its innovative point is: described plating tank comprises plating major trough and molten zinc groove, and molten zinc groove is connected with plating major trough by filter;
Arrange a telescopic bar directly over described molten zinc groove, telescopic bar bottom arranges an insoluble hanging basket, is provided with zinc ball in hanging basket.
Further, described insoluble hanging basket peripheral hardware flow-thru electrode equipment always, the positive pole of direct current energized equipment is connected with hanging basket, and negative pole is connected with molten zinc groove, has electrolytic solution in molten zinc groove.
Further, described insoluble anode is iron plate.
Further, described insoluble hanging basket is iron basket.
Further, described telescopic bar is by driving air cylinder driven.
The utility model has the advantage of: 1. the utility model by regulate the height of telescopic bar by control to immerse zinc ball in solution number, the height of zinc ion concentration in plating solution can be controlled flexibly, ensure the stable of plating solution, and it is simple to operate laborsaving, substantially increase the stability of quality product, and reduce labour intensity.
2. apply an external voltage to hanging basket and zinc ball, that add zinc ball with potential difference that is hanging basket, thus accelerate the dissolution rate of zinc ball, ensure that the supplementary of zine ion.
3. insoluble anode adopts iron plate cost low, cost-saving.
Accompanying drawing explanation
Fig. 1 is the side structure schematic diagram of the utility model alkaline zinc plating electrolytic plating pool.
Fig. 2 is the plan structure schematic diagram of the utility model alkaline zinc plating electrolytic plating pool.
Embodiment
A kind of alkaline zinc plating electrolytic plating pool as shown in Fig. 1 to 2, comprise a plating tank, positive plate, direct supply and plating piece, electroplating solution is had in plating tank, and one piece is arranged on plating tank inwall upper anode plate, also comprise peripheral hardware direct supply and a plating piece, direct supply forms loop line by wire and positive plate, plating piece, electroplating solution.
Plating tank is by electroplating major trough 1 and molten zinc groove is formed as shown in Figure 1, and molten zinc groove 2 is connected with plating major trough 1 by filter, and arrange a telescopic bar 3 directly over molten zinc groove 2, telescopic bar 3 bottom arranges an insoluble hanging basket 4, is provided with zinc ball in hanging basket 4.
Insoluble hanging basket 4 peripheral hardware flow-thru electrode equipment always as shown in Figure 2, the positive pole of direct current energized equipment is connected with hanging basket 4, and negative pole is connected with molten zinc groove 2, has electrolytic solution in molten zinc groove 2, and direct current energized equipment, hanging basket 4, electrolytic solution, molten zinc groove 2 form loop line.
The plating volume of major trough 1 and the ratio of molten zinc groove 2 volume are 2:1, and the strength of solution in the molten zinc groove of this ratio of accurate calculation is more prone to regulate, thus plating can be made more stable.
Insoluble anode in the present embodiment is iron plate, and insoluble hanging basket 4 is iron basket, and telescopic bar 3 is by driving air cylinder driven.
Its principle of work is: the utility model device changes the positive plate of plating major trough into insoluble iron plate, zinc ball to be arranged on directly over molten zinc groove in height-adjustable iron basket, by regulate highly control to immerse zinc ball in solution number, thus the height of zinc ion concentration in plating solution can be controlled flexibly, ensure that the stable of plating solution.
Claims (5)
1. an alkaline zinc plating electrolytic plating pool, comprise a plating tank, electroplating solution is had in plating tank, and one piece is arranged on plating tank inwall upper anode plate, also comprise peripheral hardware direct supply and a plating piece, direct supply forms loop line by wire and positive plate, plating piece, electroplating solution, it is characterized in that: described plating tank comprises plating major trough and molten zinc groove, and molten zinc groove is connected with plating major trough by filter;
Arrange a telescopic bar directly over described molten zinc groove, telescopic bar bottom arranges an insoluble hanging basket, is provided with zinc ball in hanging basket.
2. a kind of alkaline zinc plating electrolytic plating pool according to claim 1, is characterized in that: insoluble hanging basket peripheral hardware flow-thru electrode equipment always, and the positive pole of direct current energized equipment is connected with hanging basket, and negative pole is connected with molten zinc groove, has electrolytic solution in molten zinc groove.
3. a kind of alkaline zinc plating electrolytic plating pool according to claim 1, is characterized in that: described insoluble anode is iron plate.
4. a kind of alkaline zinc plating electrolytic plating pool according to claim 1, is characterized in that: described insoluble hanging basket is iron basket.
5. a kind of alkaline zinc plating electrolytic plating pool according to claim 1, is characterized in that: described telescopic bar is by driving air cylinder driven.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420371040.2U CN204080160U (en) | 2014-07-07 | 2014-07-07 | A kind of alkaline zinc plating electrolytic plating pool |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420371040.2U CN204080160U (en) | 2014-07-07 | 2014-07-07 | A kind of alkaline zinc plating electrolytic plating pool |
Publications (1)
Publication Number | Publication Date |
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CN204080160U true CN204080160U (en) | 2015-01-07 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201420371040.2U Expired - Lifetime CN204080160U (en) | 2014-07-07 | 2014-07-07 | A kind of alkaline zinc plating electrolytic plating pool |
Country Status (1)
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CN (1) | CN204080160U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105200498A (en) * | 2015-10-13 | 2015-12-30 | 中冶南方工程技术有限公司 | Method for controlling content of hydrogen in zinc dissolving tank for electro-galvanizing and zinc dissolving system |
WO2017084056A1 (en) * | 2015-11-19 | 2017-05-26 | 蔡慧勤 | Zinc plating device for forming zinc ring on metal fitting |
CN110144617A (en) * | 2019-06-26 | 2019-08-20 | 王宏斌 | A kind of electroplating apparatus |
-
2014
- 2014-07-07 CN CN201420371040.2U patent/CN204080160U/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105200498A (en) * | 2015-10-13 | 2015-12-30 | 中冶南方工程技术有限公司 | Method for controlling content of hydrogen in zinc dissolving tank for electro-galvanizing and zinc dissolving system |
WO2017084056A1 (en) * | 2015-11-19 | 2017-05-26 | 蔡慧勤 | Zinc plating device for forming zinc ring on metal fitting |
CN110144617A (en) * | 2019-06-26 | 2019-08-20 | 王宏斌 | A kind of electroplating apparatus |
CN110144617B (en) * | 2019-06-26 | 2021-03-30 | 杭州晨诺机械科技有限公司 | Electroplating process equipment |
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