CN204080167U - A kind of rack plating acidic zinc nickel wire - Google Patents
A kind of rack plating acidic zinc nickel wire Download PDFInfo
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- CN204080167U CN204080167U CN201420370952.8U CN201420370952U CN204080167U CN 204080167 U CN204080167 U CN 204080167U CN 201420370952 U CN201420370952 U CN 201420370952U CN 204080167 U CN204080167 U CN 204080167U
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Abstract
The utility model relates to a kind of rack plating acidic zinc nickel wire, comprises a plating tank, and this plating tank is formed by electroplating major trough and electroplating secondary groove, and the secondary groove of this plating is communicated with formation electroplate liquid circulation loop by input duct, back liquid pipeline, recycle pump with plating major trough; And plating major trough is 1.8:1 ~ 2.1:1 with the size of the secondary groove of plating, described continuous electrolysis device comprises at least one electrolysis cathode and the electrolytic anode identical with electrolysis cathode quantity, this electrolytic anode forms electrolysis cycle loop by direct supply and electrolysis cathode, electrolysis cathode and electrolytic anode are paired into one group one by one, and be arranged in parallel successively.The utility model has the advantage of: the utility model device utilizes the continuous electrolysis device in the secondary groove of plating to carry out electrolysis to the organic impurity in plating degradation production and plating solution, inorganic impurity, complete removal of impurities, so just extend the treatment cycle of tank liquor, greatly reduce the quantity discharged of waste water, reach the object reducing discharging synergy.
Description
Technical field
The utility model relates to a kind of electrolytic plating pool, especially a kind of rack plating acidic zinc nickel wire.
Background technology
Owing to have employed multiple additives, use after for some time and can produce certain degradation production, add the starting material added at ordinary times, the organic impurity in plating solution can be made, inorganic impurity increases, thus affect quality product.Therefore, need regularly (under normal circumstances monthly) to carry out down the large process of groove to tank liquor, the loss of wastewater discharge and solution will certainly be increased.Therefore, we just must develop a kind of degradation production can removed in electroplating solution, organic impurity, inorganic impurity, extend the electrolytic plating pool of the treatment cycle of tank liquor, through retrieval, do not find the electrolytic plating pool identical with the utility model.
Summary of the invention
The technical problems to be solved in the utility model is to provide a kind of degradation production can removed in electroplating solution, organic impurity, inorganic impurity, extends the electrolytic plating pool of the treatment cycle of tank liquor.
For solving the problems of the technologies described above, the technical solution of the utility model is: a kind of rack plating acidic zinc nickel wire, its innovative point is: comprise
One plating tank, this plating tank is formed by electroplating major trough and electroplating secondary groove, and the secondary groove of this plating is communicated with formation electroplate liquid circulation loop by input duct, back liquid pipeline, recycle pump with plating major trough; And plating major trough is 1.8:1 ~ 2.1:1 with the size of the secondary groove of plating;
One continuous electrolysis device, described continuous electrolysis device comprises at least one electrolysis cathode and the electrolytic anode identical with electrolysis cathode quantity, this electrolytic anode forms electrolysis cycle loop by direct supply and electrolysis cathode, and electrolysis cathode and electrolytic anode are paired into one group one by one, and be arranged in parallel successively;
Described direct supply, electrolysis cathode, electrolytic anode form loop line.
Further, described electrolysis cathode is rectangular electrolyte net, and the mesh of this electrolysis net is the rectangular opening of 2mm*2mm.
Further, described electrolysis cathode is corrugated electrolytic zinc-coated steel sheet.
Further, the electrolytic current density size of described electrolysis cathode is 0.3 ~ 0.6A/, and electrolysis voltage is 1.0 ~ 1.5V.
Further, described plating major trough can adopt integral type with the secondary groove of plating, can also adopt split type.
The utility model has the advantage of: 1. the utility model device utilizes the continuous electrolysis device in the secondary groove of plating to carry out electrolysis to the organic impurity in plating degradation production and plating solution, inorganic impurity, complete removal of impurities, so just extend the treatment cycle of tank liquor, greatly reduce the quantity discharged of waste water, reach the object reducing discharging synergy.
2. the electrolysis cathode of mesh makes the mobility of plating solution larger, and Faradaic current is more evenly distributed, and removal of impurities is more thorough.
3. the contact area of the electrolysis cathode of corrugated and plating solution is larger, and electrolysis is faster.
4. effectively can be removed the various foreign ions in tank liquor by small area analysis electrolysis, ensure the pure of plating solution.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model rack plating acidic zinc nickel wire.
Embodiment
A kind of rack plating acidic zinc nickel wire as shown in fig. 1, comprises plating tank and continuous electrolysis device.
Plating tank is formed by electroplating major trough 1 and electroplating secondary groove 5, electroplates secondary groove 5 and is communicated with formation electroplate liquid circulation loop by input duct 2, back liquid pipeline 3, recycle pump 4 and plating major trough 1; And plating major trough 1 is 1.8:1 ~ 2.1:1 with the size of the secondary groove 5 of plating, the circulation being 2:1 electroplate liquid through precision calculating plating major trough 1 and the size of the secondary groove 5 of plating reaches best.
Continuous electrolysis device comprises at least one electrolysis cathode and the electrolytic anode identical with electrolysis cathode quantity, this electrolytic anode forms electrolysis cycle loop by direct supply and electrolysis cathode, electrolysis cathode and electrolytic anode are paired into one group one by one, and be arranged in parallel successively, the electrolysis cathode of such design and electrolytic anode can form loop, make impurity-eliminating effect reach best, direct supply, electrolysis cathode, electrolytic anode form loop line.
Electrolysis cathode in the present embodiment is rectangular electrolyte net, and the mesh of this electrolysis net is the rectangular opening of 2mm*2mm, and rectangular electrolyte net is here exemplary effect certainly, and electrolysis cathode can also be corrugated electrolytic zinc-coated steel sheet.
The electrolytic current density size of electrolysis cathode is 0.3 ~ 0.6A/, and electrolysis voltage is 1.0 ~ 1.5V, carries out electrolysis and the foreign ion removing in tank liquor can be made thorough, and do not affect electroplating effect by small area analysis.
Plating major trough in the present embodiment and the secondary groove of plating can adopt integral type, can also adopt split type.
Its principle of work is: after the continuous electrolysis device energising of the utility model device, the continuous electrolysis device in the secondary groove of plating is utilized to carry out electrolysis to the organic impurity in plating degradation production and plating solution, inorganic impurity, complete removal of impurities, so just extend the treatment cycle of tank liquor, greatly reduce the quantity discharged of waste water, reach the object reducing discharging synergy.
Claims (5)
1. a rack plating acidic zinc nickel wire, is characterized in that: comprise
One plating tank, this plating tank is formed by electroplating major trough and electroplating secondary groove, and the secondary groove of this plating is communicated with formation electroplate liquid circulation loop by input duct, back liquid pipeline, recycle pump with plating major trough; And plating major trough is 1.8:1 ~ 2.1:1 with the size of the secondary groove of plating;
One continuous electrolysis device, described continuous electrolysis device comprises at least one electrolysis cathode and the electrolytic anode identical with electrolysis cathode quantity, this electrolytic anode forms electrolysis cycle loop by direct supply and electrolysis cathode, and electrolysis cathode and electrolytic anode are paired into one group one by one, and be arranged in parallel successively;
Described direct supply, electrolysis cathode, electrolytic anode form loop line.
2. a kind of rack plating acidic zinc nickel wire according to claim 1, is characterized in that: described electrolysis cathode is rectangular electrolyte net, and the mesh of this electrolysis net is the rectangular opening of 2mm*2mm.
3. a kind of rack plating acidic zinc nickel wire according to claim 1, is characterized in that: described electrolysis cathode is corrugated electrolytic zinc-coated steel sheet.
4. a kind of rack plating acidic zinc nickel wire according to claim 1, is characterized in that: the electrolytic current density size of described electrolysis cathode is 0.3 ~ 0.6A/, and electrolysis voltage is 1.0 ~ 1.5V.
5. a kind of rack plating acidic zinc nickel wire according to claim 1, is characterized in that: described plating major trough can adopt integral type with the secondary groove of plating, can also adopt split type.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420370952.8U CN204080167U (en) | 2014-07-07 | 2014-07-07 | A kind of rack plating acidic zinc nickel wire |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420370952.8U CN204080167U (en) | 2014-07-07 | 2014-07-07 | A kind of rack plating acidic zinc nickel wire |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204080167U true CN204080167U (en) | 2015-01-07 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420370952.8U Active CN204080167U (en) | 2014-07-07 | 2014-07-07 | A kind of rack plating acidic zinc nickel wire |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107227481A (en) * | 2017-07-19 | 2017-10-03 | 零八电子集团四川天源机械有限公司 | Multi-station electrical electrophoresis painting dressing groove |
-
2014
- 2014-07-07 CN CN201420370952.8U patent/CN204080167U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107227481A (en) * | 2017-07-19 | 2017-10-03 | 零八电子集团四川天源机械有限公司 | Multi-station electrical electrophoresis painting dressing groove |
| CN107227481B (en) * | 2017-07-19 | 2023-03-24 | 零八一电子集团四川天源机械有限公司 | Multi-station electrophoretic coating tank |
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