JPH04346698A - Plating device - Google Patents
Plating deviceInfo
- Publication number
- JPH04346698A JPH04346698A JP11819691A JP11819691A JPH04346698A JP H04346698 A JPH04346698 A JP H04346698A JP 11819691 A JP11819691 A JP 11819691A JP 11819691 A JP11819691 A JP 11819691A JP H04346698 A JPH04346698 A JP H04346698A
- Authority
- JP
- Japan
- Prior art keywords
- anode
- plating
- plate
- cathode plate
- plating solution
- 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.)
- Pending
Links
- 238000007747 plating Methods 0.000 title claims abstract description 55
- 238000001914 filtration Methods 0.000 claims abstract description 3
- 238000011109 contamination Methods 0.000 abstract description 3
- 239000002184 metal Substances 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 abstract 7
- 239000012528 membrane Substances 0.000 abstract 2
- 229910021645 metal ion Inorganic materials 0.000 description 5
- 230000000694 effects Effects 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000007847 structural defect Effects 0.000 description 1
Abstract
Description
【0001】0001
【産業上の利用分野】本発明はめっき装置に関し、特に
電解によってめっきをするめっき装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a plating apparatus, and more particularly to a plating apparatus that performs electrolytic plating.
【0002】0002
【従来の技術】従来のめっき装置のめっき槽の構造は、
図2に示すように、めっき槽1において被めっき物とし
ての陰極板4にめっきを施こす時、陽極板3から陰極板
4に電流が流れる。この時、陽極板3が溶解してめっき
液2中の金属濃度を保ち、陽極板3から発生する不溶解
物は、アノード袋6によって陰極板4側にあるめっき液
2には出ないような構造となっていた。まためっき液2
の浄化は、ろ過機5Aによって陰極板4側のめっき液2
を循環させて行っていた。[Prior art] The structure of the plating tank of the conventional plating equipment is as follows:
As shown in FIG. 2, when a cathode plate 4 as an object to be plated is plated in a plating bath 1, a current flows from an anode plate 3 to a cathode plate 4. At this time, the anode plate 3 is dissolved to maintain the metal concentration in the plating solution 2, and the insoluble matter generated from the anode plate 3 is prevented from flowing into the plating solution 2 on the cathode plate 4 side by the anode bag 6. It had a structure. Also, plating solution 2
The plating solution 2 on the cathode plate 4 side is purified by the filter 5A.
was being circulated.
【0003】0003
【発明が解決しようとする課題】この従来のめっき槽の
構造では、陽極板3からの不溶解物が陽極板3を包んで
いるアノード袋6に蓄積するような構造となっていた為
、陽極板3を包んでいるアノード袋6が陽極板3からの
不溶解物により目詰まりをしてしまうという欠点を有し
ていた。その結果以下に述べる不具合が発生していた。[Problems to be Solved by the Invention] In the structure of this conventional plating tank, insoluble matter from the anode plate 3 accumulates in the anode bag 6 surrounding the anode plate 3. This had the disadvantage that the anode bag 6 enclosing the plate 3 was clogged with undissolved matter from the anode plate 3. As a result, the following problems occurred.
【0004】第1に目詰りしたアノード袋6を交換する
には、めっき装置を停止して行なう必要があるため、め
っき作業再開まで長時間を要していた。First, in order to replace the clogged anode bag 6, it is necessary to stop the plating apparatus, which requires a long time until the plating operation can be restarted.
【0005】第2にめっき液中への金属イオンの補給源
であるべき陽極板3から溶出した金属イオンのアノード
袋6に滞溜する割合が高くなるため、めっき液中の金属
イオン濃度を適正値に保持する為には、外部から新たに
めっき液を補充する必要があった。Second, since the proportion of metal ions eluted from the anode plate 3, which should be a source of supply of metal ions into the plating solution, accumulates in the anode bag 6, it is necessary to maintain an appropriate concentration of metal ions in the plating solution. In order to maintain this value, it was necessary to replenish the plating solution from outside.
【0006】第3に陽極と陰極間の電圧が高(過)電圧
となり、その為アノード袋6の中に不溶解物が増加して
アノード袋6からめっき液2の中へあふれ出し、めっき
液2を汚染する場合があった。従って、めっき液の浄化
処理作業が必要となり、その分多大な工数を必要として
いた。Third, the voltage between the anode and the cathode becomes high (overvoltage), and as a result, insoluble matter increases in the anode bag 6 and overflows from the anode bag 6 into the plating solution 2. There were cases of contamination of 2. Therefore, purification of the plating solution is required, which requires a large number of man-hours.
【0007】上記不具合は、アノード袋6を採用した為
にアノード袋6内の浄化,ろ過ができないという構造的
な欠陥に起因して発生したものである。[0007] The above-mentioned problem occurred due to a structural defect in that the inside of the anode bag 6 could not be purified or filtered because the anode bag 6 was used.
【0008】[0008]
【課題を解決するための手段】本発明のめっき装置は、
めっき液を満たすめっき槽と、このめっき槽内に設置さ
れる陽極板と陰極板と、この陽極板と陰極板とを分離す
る隔膜と、この隔膜により分離された前記陽極板側のめ
っき液をろ過するためのろ過機とを含むものである。[Means for Solving the Problems] The plating apparatus of the present invention includes:
A plating tank filled with a plating solution, an anode plate and a cathode plate installed in the plating tank, a diaphragm separating the anode plate and the cathode plate, and a plating solution on the anode plate side separated by the diaphragm. and a filter for filtering.
【0009】[0009]
【実施例】次に本発明について図面を参照して説明する
。図1は本発明の一実施例の模式断面図である。DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, the present invention will be explained with reference to the drawings. FIG. 1 is a schematic cross-sectional view of one embodiment of the present invention.
【0010】図1においてめっき装置は、めっき液を満
たすめっき槽5とこのめっき槽5内に設置される陽極板
3と陰極板4と、この陽極板3と陰極板4とを分離する
隔膜7と、陽極板側のめっき液をろ過するろ過機5とか
ら主に構成されている。In FIG. 1, the plating apparatus includes a plating tank 5 filled with a plating solution, an anode plate 3 and a cathode plate 4 installed in the plating tank 5, and a diaphragm 7 separating the anode plate 3 and the cathode plate 4. and a filter 5 that filters the plating solution on the anode plate side.
【0011】被めっき物である陰極板4にめっきを施こ
す時、陽極板3から陰極板4に電流が流れる。この時陽
極板3が溶解してめっき液2中の金属濃度を一定に保つ
ようにするが、陽極板3の不溶解物が陽極板3側のめっ
き液2中に生成する。この陽極板3側のめっき液中の不
溶解物をろ過機5によってろ過して陰極板4側のめっき
液2中に戻す。When plating the cathode plate 4, which is the object to be plated, a current flows from the anode plate 3 to the cathode plate 4. At this time, the anode plate 3 is dissolved to keep the metal concentration in the plating solution 2 constant, but undissolved matter of the anode plate 3 is generated in the plating solution 2 on the anode plate 3 side. Insoluble matter in the plating solution on the anode plate 3 side is filtered by a filter 5 and returned to the plating solution 2 on the cathode plate 4 side.
【0012】このように本実施例においては、隔膜7に
よって陽極板3と陰極板4との間を仕切って槽を二分し
て、陽極板3側のめっき液2をろ過することにより、陽
極板3から発生する不溶解物を常時取り除き、かつろ過
液が陰極板4側から陽極板3側に流れる為、陽極板3か
ら生成する不溶解物が陰極板4側のめっき液2中に逆流
することを防ぐことができる。As described above, in this embodiment, the anode plate 3 and the cathode plate 4 are partitioned by the diaphragm 7 to divide the tank into two, and the plating solution 2 on the anode plate 3 side is filtered. Since the insoluble matter generated from the anode plate 3 is constantly removed and the filtrate flows from the cathode plate 4 side to the anode plate 3 side, the insoluble matter generated from the anode plate 3 flows back into the plating solution 2 on the cathode plate 4 side. This can be prevented.
【0013】[0013]
【発明の効果】以上説明したように本発明は、陽極板側
と陰極板側とを隔膜によって槽を分けて、陽極板側のめ
っき液を常時ろ過することにより陽極板から発生する不
溶解物を常時取り除くことができるので、陽極板から溶
けた金属イオンが効率的に混合されるため、めっき液濃
度の管理におけるめっき液の補充量を少くできる。また
、陽極板の不溶解物によるめっき浴の汚染もなくなるば
かりでなく、従来必要であったアノード袋の取換えが不
要になる。更にめっき液の浄化処理に要していた時間を
減少させることができるという効果を有する。Effects of the Invention As explained above, the present invention separates the anode plate side and the cathode plate side into tanks with a diaphragm, and constantly filters the plating solution on the anode plate side, thereby eliminating insoluble matter generated from the anode plate. Since metal ions dissolved from the anode plate can be removed at all times, the metal ions dissolved from the anode plate can be mixed efficiently, so that the amount of plating solution replenishment can be reduced when managing the plating solution concentration. Furthermore, not only is there no contamination of the plating bath by undissolved matter on the anode plate, but there is also no need to replace the anode bag, which was previously necessary. Furthermore, it has the effect of reducing the time required for purifying the plating solution.
【図1】本発明の一実施例の模式断面図。FIG. 1 is a schematic cross-sectional view of one embodiment of the present invention.
【図2】従来のめっき装置の模式断面図。FIG. 2 is a schematic cross-sectional view of a conventional plating apparatus.
1 めっき槽 2 めっき液 3 陽極板 4 陰極板 5,5A ろ過機 6 アノード袋 7 隔膜 1 Plating tank 2 Plating solution 3 Anode plate 4 Cathode plate 5,5A filter machine 6 Anode bag 7 Diaphragm
Claims (1)
っき槽内に設置される陽極板と陰極板と、この陽極板と
陰極板とを分離する隔膜と、この隔膜により分離された
前記陽極板側のめっき液をろ過するためのろ過機とを含
むことを特徴とするめっき装置。1. A plating tank filled with a plating solution, an anode plate and a cathode plate installed in the plating tank, a diaphragm separating the anode plate and the cathode plate, and the anode plate separated by the diaphragm. A plating device comprising a filter for filtering a plating solution on the side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11819691A JPH04346698A (en) | 1991-05-23 | 1991-05-23 | Plating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11819691A JPH04346698A (en) | 1991-05-23 | 1991-05-23 | Plating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04346698A true JPH04346698A (en) | 1992-12-02 |
Family
ID=14730551
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11819691A Pending JPH04346698A (en) | 1991-05-23 | 1991-05-23 | Plating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04346698A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2022199168A1 (en) * | 2021-03-25 | 2022-09-29 | 宁德时代新能源科技股份有限公司 | Filtration mechanism, and apparatus for producing conductive material |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54132439A (en) * | 1978-04-05 | 1979-10-15 | Furukawa Electric Co Ltd:The | Electroplating method |
JPS55161096A (en) * | 1979-06-04 | 1980-12-15 | Furukawa Electric Co Ltd:The | Continuous electroplating method |
-
1991
- 1991-05-23 JP JP11819691A patent/JPH04346698A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54132439A (en) * | 1978-04-05 | 1979-10-15 | Furukawa Electric Co Ltd:The | Electroplating method |
JPS55161096A (en) * | 1979-06-04 | 1980-12-15 | Furukawa Electric Co Ltd:The | Continuous electroplating method |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2022199168A1 (en) * | 2021-03-25 | 2022-09-29 | 宁德时代新能源科技股份有限公司 | Filtration mechanism, and apparatus for producing conductive material |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 19970805 |