JPH059798A - Method for dissolving metal powder in electro-plating - Google Patents

Method for dissolving metal powder in electro-plating

Info

Publication number
JPH059798A
JPH059798A JP15906991A JP15906991A JPH059798A JP H059798 A JPH059798 A JP H059798A JP 15906991 A JP15906991 A JP 15906991A JP 15906991 A JP15906991 A JP 15906991A JP H059798 A JPH059798 A JP H059798A
Authority
JP
Japan
Prior art keywords
metal powder
plating solution
tank
suspension
plating
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
Application number
JP15906991A
Other languages
Japanese (ja)
Inventor
Yukihiko Uchiyama
幸彦 内山
Takaaki Ishikawa
貴章 石川
Kaoru Mizumoto
薫 水本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP15906991A priority Critical patent/JPH059798A/en
Publication of JPH059798A publication Critical patent/JPH059798A/en
Pending legal-status Critical Current

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  • Electroplating Methods And Accessories (AREA)

Abstract

PURPOSE:To extremely easily dissolve the metal powder in electroplating without need for a special device such as a metal powder recovery means. CONSTITUTION:A part of the metal powder charged into a solution tank 2 is mixed into a plating soln. to be sent to a suspended matter treating system 4 consisting of a cushion tank 5, a filter 6, a dehydrator 7, etc., and discharged, and a part of the dissolving action in the solution tank is assigned to the suspended matter treating system.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は電気めっきにおいて、
めっき液へ金属イオンを補給する際の金属粉の溶解方法
に関するものである。
This invention relates to electroplating,
The present invention relates to a method for dissolving metal powder when supplying metal ions to a plating solution.

【0002】[0002]

【従来の技術】例えば鉄系電気めっきは、めっき液中の
Fe2+イオンの析出反応により電気めっきを行うものであ
るが、めっき処理の経過に伴いめっき液中のFe2+イオン
は酸化反応によりFe3+イオンを生成することになる。従
って、このめっき液はFe2+イオンを補給するとともにFe
3+イオンを還元する必要があり、一般的には攪拌式や流
動式等の溶解槽に前記Fe3+イオンを含むめっき液を循環
させ、これに鉄粉を投入しながらこの鉄粉を溶解させる
ことによりFe 2+イオンの補給とFe3+イオンの還元を行い
めっき液の再使用を図っている。
2. Description of the Related Art For example, iron-based electroplating is performed in a plating solution.
Fe2+Electroplating is performed by ion precipitation reaction.
However, as the plating process progresses, Fe in the plating solution2+ion
Is Fe due to the oxidation reaction3+It will generate ions. Servant
This plating solution is Fe2+Fe is replenished with ions
3+Ions need to be reduced and are typically stirred or flow
The Fe is added to the dynamic tank3+Circulate the plating solution containing ions
Then, while iron powder is added to this, this iron powder is dissolved
By Fe 2+Ion supply and Fe3+To reduce the ions
We are trying to reuse the plating solution.

【0003】このようなめっき液の処理は、他の金属の
電気めっきにおいても上述鉄系電気めっきの場合と還元
作用を除けば大きく変わるものではない。そしてこの処
理の際、めっき液には種々の懸濁物が混入しているた
め、溶解槽からめっき設備に戻される過程で濾過装置等
から構成される懸濁物処理系統によってめっき液中の懸
濁物を除去する。
Such a treatment of the plating solution does not greatly change in the electroplating of other metals as well as in the case of the above-mentioned iron-based electroplating except for the reducing action. Since various suspensions are mixed in the plating solution during this treatment, the suspension in the plating solution is suspended by a suspension treatment system consisting of a filtration device etc. in the process of returning from the dissolution tank to the plating equipment. Remove turbidity.

【0004】一方、溶解槽に投入した金属粉は投入量の
制御性等の見地から可及的速やかに溶解させ、懸濁物処
理系統にはできるだけ逸出しないようにしていた。その
ために、例えば特開昭59−126799号公報に示される如
く、めっき液を循環する際にキャリオーバする未反応粉
または粒を回収して反応槽にリサイクルする方法があ
る。
On the other hand, the metal powder charged into the melting tank was dissolved as soon as possible from the viewpoint of controllability of the amount charged and the like, so as not to escape to the suspension treatment system as much as possible. Therefore, as disclosed in, for example, Japanese Patent Application Laid-Open No. 59-126799, there is a method of recovering unreacted powder or particles that carry over when circulating a plating solution and recycling to the reaction tank.

【0005】[0005]

【発明が解決しようとする課題】溶解槽に投入された金
属粉を速やかに、しかも完全に溶解しようとすればそれ
だけ攪拌機等の容量が大きくなり、必然的に溶解槽自体
も大きなものになる。また前記特開昭59−126799号公報
に示された方法は、未反応粉または粒を回収するための
装置が必要であり、この場合も完全に回収しようとすれ
ばかなり大掛かりな装置を設置しなければならず、その
保全等も併せて考慮すると経済的にも大きな負担となり
問題である。
[Problems to be Solved by the Invention] If the metal powder charged into the melting tank is to be dissolved quickly and completely, the capacity of the stirrer or the like will be increased, and the melting tank itself will be inevitably large. Further, the method disclosed in JP-A-59-126799 requires a device for recovering unreacted powder or particles, and even in this case, if a complete recovery is attempted, a considerably large device is installed. It must be taken into consideration, and considering the maintenance and so on, it will be a great financial burden and a problem.

【0006】この発明は従来から使用されている溶解槽
と懸濁物処理系統をそのまま使用し、経済的にも工程的
にも何ら負担の増加を伴わず、溶解槽に投入された鉄粉
を完全に溶解できる方法を提供することを目的とするも
のである。
The present invention uses the dissolution tank and the suspension treatment system which have been conventionally used as they are, and the iron powder put into the dissolution tank is added without any increase in the burden economically and in process. The object is to provide a method capable of completely dissolving.

【0007】[0007]

【課題を解決するための手段】この発明による電気めっ
きにおける金属粉の溶解方法は、金属粉の溶解槽とこの
溶解槽から送出されるめっき液中の懸濁物を除去するた
めの懸濁物処理系統とを有するめっき液処理設備を用い
て前記溶解槽内のめっき液に金属粉を投入しながらこの
金属粉を溶解する電気めっきにおける金属粉の溶解方法
であって、前記投入された金属粉の溶解を前記溶解槽内
と前記懸濁物処理系統内とに分担させて行うようにし
て、上述従来の技術の課題を解決した。
A method for dissolving metal powder in electroplating according to the present invention comprises a metal powder dissolving tank and a suspension for removing a suspension in a plating solution delivered from the dissolving tank. A method for dissolving metal powder in electroplating, which comprises dissolving a metal powder into a plating solution in the dissolution tank by using a plating solution treatment facility having a treatment system, wherein the introduced metal powder The problem of the above-mentioned conventional technique was solved by sharing the above-mentioned dissolution in the dissolution tank and in the suspension treatment system.

【0008】[0008]

【作 用】溶解槽からめっき設備に戻されるめっき液
は、前述のように懸濁物を除去するために濾過装置等の
懸濁物処理系統を通過させるが、この過程で相当激しい
攪拌が行われることに着目してこの発明がなされたもの
である。すなわち、溶解槽内のめっき液に投入された金
属粉は、溶解槽内で完全に溶解される必要はなく、一部
の未溶解金属粉がめっき設備に戻されるめっき液に混入
した状態で逸出しても、この逸出した金属粉は最終的に
廃棄される懸濁物と共に廃棄されるのではなく、それま
での間に完全に溶解させるよう懸濁物処理系統が溶解槽
と同様な作用を及ぼすものと考えた。
[Operation] The plating solution returned from the dissolution tank to the plating equipment is passed through a suspension treatment system such as a filtration device in order to remove the suspension as described above. This invention was made with a focus on what is said. In other words, the metal powder added to the plating solution in the melting tank does not need to be completely dissolved in the melting tank, and some undissolved metal powder is lost in the plating solution returned to the plating equipment. Even if it is released, this escaped metal powder is not discarded together with the suspension that is finally discarded, but the suspension treatment system works in the same way as the dissolution tank to completely dissolve it until then. I thought that it would cause.

【0009】そこでこの発明は、溶解槽内のめっき液に
投入された金属粉の溶解を、溶解槽内と懸濁物処理系統
内とに分担させるようにした。またその分担割合には特
に制限はなく、むしろ懸濁物処理系統に設置された機器
ならびに配管が、通過する金属粉によってあまりひどく
摩滅しない程度であれば十分に実用化可能であることも
わかった。
Therefore, in the present invention, the dissolution of the metal powder charged in the plating solution in the dissolution tank is shared between the dissolution tank and the suspension treatment system. It was also found that there is no particular limitation on the share, and rather the equipment and pipes installed in the suspension treatment system can be put to practical use sufficiently if they do not become worn out too much by the passing metal powder. ..

【0010】[0010]

【実施例】図1に溶解槽と懸濁物処理系統を含む鉄系電
気めっき液処理設備の概要を示す。図において1はサー
キュレーションタンクであり、このタンクから図示省略
した電気めっきセルにめっき液を送給し、また電気めっ
きセルから戻されるめっき液を受け入れる。
EXAMPLE FIG. 1 shows an outline of iron-based electroplating solution treatment equipment including a dissolution tank and a suspension treatment system. In the figure, reference numeral 1 denotes a circulation tank from which a plating solution is fed to an electroplating cell (not shown) and receives a plating solution returned from the electroplating cell.

【0011】サーキュレーションタンク1内のめっき液
は、その一部が配管10を介して溶解槽2に送られ、この
溶解槽2内で前述のようにFe2+イオンが補給されるとと
もにFe3+イオンが還元される。なおこの例の溶解槽2は
攪拌式であり、攪拌機3により投入された鉄粉とめっき
液を攪拌しているが、これは流動式等の他の方式の溶解
槽であってもよい。
A part of the plating solution in the circulation tank 1 is sent to the dissolution tank 2 through the pipe 10, and in the dissolution tank 2, Fe 2+ ions are replenished and Fe 3 + is added as described above. + Ions are reduced. The dissolution tank 2 in this example is a stirring type, and the iron powder and the plating solution charged by the stirrer 3 are stirred, but this may be a dissolution tank of another type such as a fluid type.

【0012】そして、投入された鉄粉は一部未溶解のま
まめっき設備側に戻されるめっき液に混入して配管11に
より懸濁物処理系統4に送られる。なお、従来はこの懸
濁物処理系統4には回収手段等により鉄粉が混入してい
ないめっき液が送られていたが、この発明では溶解槽2
から逸出した鉄粉が混入していることは前述のとおりで
ある。
Then, the iron powder that has been introduced is mixed in the plating solution returned to the plating equipment side while being partially undissolved and sent to the suspension treatment system 4 through the pipe 11. Incidentally, in the past, a plating solution containing no iron powder was sent to the suspension treatment system 4 by a recovery means or the like.
As mentioned above, the iron powder that escaped from the product is mixed.

【0013】懸濁物処理系統4では、先ずクッションタ
ンク5に鉄粉の混入しためっき液(以下この状態の液を
単にめっき液という)を貯溜する。このクッションタン
ク5は溶解槽2と懸濁物処理系統4との間のバッファと
しての働きをするものである。このクッションタンク5
で混入している鉄粉のごく一部が溶解される。続いてめ
っき液は配管12を通って濾過機6に送給される。この濾
過機6は、例えばリーフフィルタの如く微細な懸濁物が
除去可能なものであり、2台または複数台を交互に使用
する。鉄粉はこの濾過機6内でほとんどが溶解される。
ここで、濾過機6を通過した清浄なめっき液は配管13に
よりサーキュレーションタンク1に返送して再度使用す
ることになる。
In the suspension treatment system 4, first, the cushion tank 5 stores a plating solution containing iron powder (hereinafter, the solution in this state is simply referred to as a plating solution). The cushion tank 5 functions as a buffer between the dissolution tank 2 and the suspension treatment system 4. This cushion tank 5
A small part of the iron powder mixed in is dissolved. Subsequently, the plating solution is sent to the filter 6 through the pipe 12. The filter 6 is capable of removing fine suspended matter, such as a leaf filter, and two or more filters are alternately used. Most of the iron powder is dissolved in the filter 6.
Here, the clean plating solution that has passed through the filter 6 is returned to the circulation tank 1 through the pipe 13 and used again.

【0014】一方、濾過機6によって捕捉された懸濁物
は、濾過機6の濾布がある程度目詰まりした時点で配管
13から分岐された洗浄用配管14を介して供給される清浄
なめっき液によって洗浄され、このめっき液と共にスラ
リ状となって配管15により脱水機7に送られる。ここま
で処理された懸濁物には鉄粉はほとんど残っていない
が、たとえ残っていても脱水機7での脱水中に完全に溶
解される。そして脱水後の懸濁物はケーキとして取出
し、コンベヤ8により系外に搬出して廃棄する。なお、
脱水機7により分離されためっき液は配管16を介して再
度クッションタンク5に戻される。
On the other hand, when the filter cloth of the filter 6 is clogged to some extent, the suspension captured by the filter 6 is piped.
It is cleaned with a clean plating solution supplied through a cleaning pipe 14 branched from 13, and is sent to the dehydrator 7 through a pipe 15 in the form of a slurry together with this plating solution. Almost no iron powder remains in the suspension treated up to this point, but even if it remains, it will be completely dissolved during dehydration in the dehydrator 7. Then, the suspension after dehydration is taken out as a cake, carried out of the system by the conveyor 8 and discarded. In addition,
The plating solution separated by the dehydrator 7 is returned to the cushion tank 5 again via the pipe 16.

【0015】このように溶解槽2から逸出してめっき液
と共に懸濁物処理系統4に供給された鉄粉は、その処理
過程で完全に溶解できるため、懸濁物のケーキに混入し
て廃棄されるうれいは全くない。攪拌式の溶解槽内のめ
っき液に2000gの鉄粉(めっき液1m3あたり、以下も同
様)を投入して溶解したが、この際に投入した鉄粉の一
部がめっき液に混入して懸濁物処理系統へ逸出するよう
にした。この場合、溶解槽出側の逸出鉄粉量は 305g
(投入量の 15.25%)であった。そして懸濁物処理系統
各部の鉄粉残量を調査した。その結果、クッションタン
ク出側では 295g(溶解量は逸出量の 3.3%)で、濾過
機から排出されたスラリ状の液中には溶解槽から送出さ
れためっき液量換算で約7g、すなわち濾過機での溶解
量は288gで逸出量の94.4%であった。また、脱水機か
ら排出される懸濁物のケーキ中にも、クッションタンク
に戻されるめっき液中にも鉄粉が残留している痕跡はな
かった。
The iron powder thus escaped from the dissolution tank 2 and supplied to the suspension treatment system 4 together with the plating solution can be completely dissolved during the treatment process, and therefore is mixed with the suspension cake and discarded. There is no joy to be told. 2000 g of iron powder (per 1 m 3 of plating solution, the same applies below) was added to the plating solution in the stirring type dissolution tank and dissolved, but part of the iron powder added at this time was mixed in the plating solution. Escape to the suspension treatment system. In this case, the amount of iron powder escaped from the melting tank is 305g.
(15.25% of the input amount). Then, the amount of iron powder remaining in each part of the suspension treatment system was investigated. As a result, it was 295g on the outlet side of the cushion tank (dissolved amount was 3.3% of the escaped amount), and about 7g in terms of the amount of plating liquid sent from the dissolution tank in the slurry-like liquid discharged from the filter, The amount dissolved in the filter was 288 g, which was 94.4% of the amount released. Further, there was no trace of iron powder remaining in the cake of the suspension discharged from the dehydrator or in the plating solution returned to the cushion tank.

【0016】以上の結果から、溶解槽からめっき液と共
に鉄粉を懸濁物処理系統に逸出させても、この鉄粉は懸
濁物の処理過程で完全に溶解されることが確認できた。
なお、溶解槽から逸出する鉄粉の量は正確に制御する必
要はなく、およその量の制御はめっき液の出側配管の位
置を調整する等の簡単な手段を講ずればよいものであ
る。
From the above results, it was confirmed that the iron powder was completely dissolved in the process of treating the suspension even if the iron powder was allowed to escape from the dissolution tank to the suspension treatment system together with the plating solution. ..
The amount of iron powder that escapes from the melting tank does not have to be accurately controlled, and the approximate amount can be controlled by simple means such as adjusting the position of the plating solution outlet piping. is there.

【0017】また以上の説明の中では鉄系電気めっきを
対象に説明したが、これは他のH+ イオンとイオン化傾
向の差の大きい金属、例えばZnやNi等の金属の電気めっ
きにも適用されることはもちろんである。
In the above description, iron-based electroplating has been described, but this is also applicable to electroplating of metals having a large difference in ionization tendency from other H + ions, for example, metals such as Zn and Ni. Of course it will be done.

【0018】[0018]

【発明の効果】この発明による電気めっきにおける金属
粉の溶解方法を実施すれば、溶解槽内のめっき液に投入
された金属粉をこの槽内で完全に溶解する必要がなくな
り、従って金属粉の回収手段等の特別な装置を必要とせ
ず、従来の設備をそのまま使用でき、経済的にも極めて
有利なものである。
When the method for dissolving metal powder in electroplating according to the present invention is carried out, it is not necessary to completely dissolve the metal powder charged in the plating solution in the melting tank, and therefore the metal powder It does not require a special device such as a recovery means and the conventional equipment can be used as it is, which is extremely economically advantageous.

【0019】しかも、溶解槽内と懸濁物処理系統内で行
う金属粉の溶解の分担割合にはほとんど制約がないた
め、溶解作業が至極単純になる等の利点もある。
Moreover, since there is almost no restriction on the share of the dissolution of the metal powder in the dissolution tank and in the suspension treatment system, there is an advantage that the dissolution work is extremely simple.

【図面の簡単な説明】[Brief description of drawings]

【図1】溶解槽と懸濁物処理系統を含む鉄系電気めっき
液処理設備の概要説明図である。
FIG. 1 is a schematic explanatory diagram of an iron-based electroplating solution treatment facility including a dissolution tank and a suspension treatment system.

【符号の説明】[Explanation of symbols]

1 サーキュレーションタンク 2 溶解槽 3 攪拌機 4 懸濁物処理系統 5 クッションタンク 6 濾過機 7 脱水機 8 コンベヤ 10〜16 配管 1 Circulation tank 2 Dissolution tank 3 Stirrer 4 Suspension processing system 5 Cushion tank 6 Filtration machine 7 Dehydrator 8 Conveyor 10-16 Piping

Claims (1)

【特許請求の範囲】 【請求項1】 金属粉の溶解槽とこの溶解槽から送出さ
れるめっき液中の懸濁物を除去するための懸濁物処理系
統とを有するめっき液処理設備を用いて前記溶解槽内の
めっき液に金属粉を投入しながらこの金属粉を溶解する
電気めっきにおける金属粉の溶解方法であって、前記投
入された金属粉の溶解を前記溶解槽内と前記懸濁物処理
系統内とに分担させて行うことを特徴とする電気めっき
における金属粉の溶解方法。
Claim: What is claimed is: 1. A plating solution treatment facility having a metal powder dissolving tank and a suspension treatment system for removing a suspension in the plating solution delivered from the dissolving tank. A method for dissolving metal powder in electroplating, wherein the metal powder is dissolved while adding the metal powder to the plating solution in the dissolution tank, wherein the dissolution of the introduced metal powder is suspended in the dissolution tank and in the suspension. A method for melting metal powder in electroplating, characterized in that the method is shared with the inside of a material processing system.
JP15906991A 1991-06-28 1991-06-28 Method for dissolving metal powder in electro-plating Pending JPH059798A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15906991A JPH059798A (en) 1991-06-28 1991-06-28 Method for dissolving metal powder in electro-plating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15906991A JPH059798A (en) 1991-06-28 1991-06-28 Method for dissolving metal powder in electro-plating

Publications (1)

Publication Number Publication Date
JPH059798A true JPH059798A (en) 1993-01-19

Family

ID=15685541

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15906991A Pending JPH059798A (en) 1991-06-28 1991-06-28 Method for dissolving metal powder in electro-plating

Country Status (1)

Country Link
JP (1) JPH059798A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0669410A1 (en) * 1994-02-28 1995-08-30 Kawasaki Steel Corporation Apparatus for continuously dissolving metal powder for use in plating and method of dissolving nickel metal using same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0669410A1 (en) * 1994-02-28 1995-08-30 Kawasaki Steel Corporation Apparatus for continuously dissolving metal powder for use in plating and method of dissolving nickel metal using same

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