JPH03243798A - Supplying method for iron ion in electroplating iron-based alloy - Google Patents

Supplying method for iron ion in electroplating iron-based alloy

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Publication number
JPH03243798A
JPH03243798A JP3881690A JP3881690A JPH03243798A JP H03243798 A JPH03243798 A JP H03243798A JP 3881690 A JP3881690 A JP 3881690A JP 3881690 A JP3881690 A JP 3881690A JP H03243798 A JPH03243798 A JP H03243798A
Authority
JP
Japan
Prior art keywords
iron
chips
chip
tank
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
JP3881690A
Other languages
Japanese (ja)
Inventor
Hirohiko Sakai
堺 裕彦
Masatoshi Iwai
正敏 岩井
Shinobu Nakayama
忍 中山
Hiroaki Nakano
博昭 中野
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel Ltd
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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP3881690A priority Critical patent/JPH03243798A/en
Publication of JPH03243798A publication Critical patent/JPH03243798A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To always stabilize the concn. of Fe ion in plating liquid at constant value by circulating the plating liquid in the specified conditions through a dissolving tank of Fe chips for replenishing Fe ions contained in the plating liquid in an Fe-based plating device equipped with an insoluble anode. CONSTITUTION:In order to replenish reduction of Fe<2+> ion in plating liquid M in an Fe-based plating device equipped with an insoluble anode, this plating liquid M whose Fe<2+> ions are reduced is supplied from an inlet 12 in the lower part of a dissolving tank 1 packed with Fe chips T and raised at the relative velocity of at least >=3 m/min through the Fe chip layer T. The Fe chips are dissolved and the concn. of Fe<2+> is raised to the specified % and this plating liquid is circulated and supplied to the plating tank. In this case, the relation of b/a <=3 is held between the diameter (a) of the Fe chip layer in the Fe chip packing tank 1 and height (b). Further, the concn. of Fe<3+> of the plating liquid in the inlet 12 is regulated to >=5 g/l. Thereby Fe chips T are rapidly dissolved into plating liquid. The Fe chips pulverized by dissolution are discharged from the dissolving tank 1 by rotation of a screw rod 8. Thereby passage of plating liquid supplied from the inlet 12 is enhanced.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は鉄系合金電気めっきにおける鉄イオン供給方法
に関し、さらに詳しくは、鉄チップ溶解檜内の鉄充填層
の鉄チップの溶解量を安定させ、Fe’+の還元を優先
させて溶解し、鉄系合金電気めっき槽に鉄イオンを供給
する方法に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for supplying iron ions in iron-based alloy electroplating, and more specifically, to a method for stabilizing the amount of iron chips dissolved in an iron packed bed in an iron chip melting chamber. The present invention relates to a method of supplying iron ions to an iron-based alloy electroplating tank by dissolving Fe'+ with priority given to reduction.

[従来技術] 一般に、従来より不溶性陽極を使用する電気めっきにお
いては、めっきの進行により減少する金属イオンをめっ
き液中に供給するために、めっきすべき金属をめっき液
により溶解することが行なわれてきている。
[Prior Art] Generally, in electroplating using an insoluble anode, the metal to be plated is dissolved in the plating solution in order to supply the metal ions that decrease as the plating progresses to the plating solution. It's coming.

しかして、不溶性陽極を使用する鉄系合金電気めっきに
おいては、陽極ではFe”イオンがFe針ビイオン酸化
されて、F e”イオンの濃度が高くなると、めっき電
流効率が低下してめっき表面外観劣化等の問題が生じる
。そのため、Fe”+イオンをめっき槽に供給する際に
は、同時にめっき液中のPe′3十イオアイオンを行わ
なければならない。
However, in iron-based alloy electroplating using an insoluble anode, Fe" ions are oxidized by Fe needle bioions at the anode, and when the concentration of Fe" ions increases, the plating current efficiency decreases and the appearance of the plating surface deteriorates. Problems such as this arise. Therefore, when Fe''+ ions are supplied to the plating tank, it is necessary to ionize Pe'30 ions in the plating solution at the same time.

そして、めっき液による金属鉄の溶解反応には、水素発
生溶解反応とFe3+イオン還元溶解反応の2つの反応
があり、この2つの反応が共存している。
The dissolution reaction of metallic iron by the plating solution includes two reactions: a hydrogen generation dissolution reaction and an Fe3+ ion reduction dissolution reaction, and these two reactions coexist.

また、金属鉄の水素発生溶解反応とFe3+イオン還元
溶解反応を電気化学的に比較すると、反応の推進力であ
る酸化還元電位より通常はFe3イオン還元溶解反応の
方か扇かに生じ易いことがわかる。
In addition, when comparing electrochemically the hydrogen generation dissolution reaction and the Fe3+ ion reduction and dissolution reaction of metallic iron, it is found that the Fe3 ion reduction and dissolution reaction is usually more likely to occur than the redox potential which is the driving force of the reaction. Recognize.

実際に、一定量のFe’+イオンが存在する場合には、
Fe5fイオン還元溶解反応が優先するため、Fe’→
イオン還元効率は90%以上であり、鉄溶解量も多く安
定している。このFe’+イオン還元効率とは、鉄の溶
解反応に占めるFe3寸イオン還元溶解反応の割合であ
る。
In fact, if a certain amount of Fe'+ ions exist,
Since the Fe5f ion reduction and dissolution reaction takes precedence, Fe'→
The ion reduction efficiency is 90% or more, and the amount of iron dissolved is large and stable. This Fe′+ ion reduction efficiency is the ratio of the Fe 3 size ion reduction and dissolution reaction to the iron dissolution reaction.

しかし、Fe3 +イオン濃度が低くなった場合、鉄溶
解量およびFe3+イオン還元効率が低下するという問
題がある。即ち、鉄溶解槽の一方からめっき液を圧入す
ることにより鉄チブプを溶解すると、Fe3士イオン還
元溶解反応が生じるため、めっき液中のFe3+イオン
濃度は鉄溶解槽の入側から出側の方にかけて徐々に低く
なっているのである。
However, when the Fe3+ ion concentration becomes low, there is a problem that the amount of dissolved iron and the Fe3+ ion reduction efficiency decrease. In other words, when the iron chips are dissolved by pressurizing the plating solution from one side of the iron dissolution tank, a reduction and dissolution reaction of Fe3+ ions occurs, so the Fe3+ ion concentration in the plating solution increases from the inlet side to the outlet side of the iron dissolution tank. It gradually decreases over time.

また、鉄溶解槽中の鉄チップの溶解を長時間にわたり連
続的に行うと、鉄充填層を流れるめっき液の偏流により
鉄チップが不均一に溶解したり、Fe”イオン還元効率
の低下および鉄溶解量が低下するという問題が発生する
。このような鉄充填層を流れるめっき液の偏流の原因と
しては、溶解により微細化した鉄チップか形状の大きな
鉄チップの間に入り込み、不均一な空隙が形成されるこ
とによるものと考えられる。
Furthermore, if the iron chips in the iron melting tank are melted continuously over a long period of time, the iron chips may be unevenly melted due to the uneven flow of the plating solution flowing through the iron packed bed, and the Fe" ion reduction efficiency may be reduced. A problem arises in that the amount of dissolution decreases.The cause of this uneven flow of the plating solution flowing through the iron packed bed is that it gets between the iron chips that have become finer due to melting or the iron chips that have a larger shape, resulting in uneven voids. This is thought to be due to the formation of

鉄溶解槽中の鉄チップを長時間にわたり溶解を行なうと
、Fe3”イオン還元効率および鉄溶解量が低下する原
因としては、めっき液の偏流以外に、鉄チップの溶解反
応により生成した水素ガスが鉄チップ表面に付着し、F
e3+イオンの鉄チップ表面への拡散を阻害しているも
のと考えられる。
When iron chips in an iron melting tank are melted for a long time, the Fe3" ion reduction efficiency and amount of iron dissolution decreases. In addition to the uneven flow of the plating solution, hydrogen gas generated by the dissolution reaction of the iron chips is also a cause. It adheres to the iron chip surface and F
This is thought to inhibit the diffusion of e3+ ions to the surface of the iron chip.

[発明が解決しようとする課題] 本発明は上記に説明した従来における鉄系合金電気めっ
きに際して、めっき槽に鉄イオンを供給する場合の種々
の問題点に鑑み、本発明者が鋭意研究を行い、検討を重
ねた結果、鉄チップ溶解層の径と高さとの比を規定し、
また、鉄チップを溶解するための鉄チップ溶解檀入側の
めっき液のFe3+イオノ濃度および鉄チップとめっき
液の相対流速を一定値以上とすることにより、鉄チップ
溶解層中の鉄チップの溶解量を安定化させ、かつ、Fe
’イオン還元を優先させることができる鉄系合金電気め
っきにおける鉄イオン供給方法を開発したのである。
[Problems to be Solved by the Invention] The present invention is based on the inventor's extensive research in view of the various problems encountered when supplying iron ions to the plating tank during the conventional iron-based alloy electroplating described above. As a result of repeated studies, we determined the ratio between the diameter and height of the iron chip dissolution layer,
In addition, by setting the Fe3+ ion concentration of the plating solution on the side where the iron chips are melted and the relative flow rate between the iron chips and the plating solution to be above a certain value, the iron chips in the iron chip dissolution layer can be dissolved. The amount is stabilized, and Fe
'We have developed an iron ion supply method for iron-based alloy electroplating that can give priority to ion reduction.

E問題点を解決するための手段] 本発明に係る鉄系合金電気めっきにおける鉄イノ オン供給方法は、 (1)鉄系合金電気めっきにおいて、めっき槽に鉄イオ
ンを供給するために鉄チップを充填した鉄チップ溶解槽
の下方からめっき液を圧入して鉄チップを溶解する場合
に、鉄チップ溶解槽内の円筒軟鉄チップ充填層の径a 
(mm)と高さb(IIIIll)との関係がb / 
a≦3を満たし、かつ、鉄チップ溶解槽入側のめっき液
中のp e3 +濃度を5g/l以上、鉄チップ溶解槽
中の鉄チップと圧入するめっき液との相対流速を3 m
/min以上とすることを特徴とする鉄系合金電気めっ
きにおける鉄イオン供給方法を第1の発明とし、 (2)鉄系合金電気めっきにおいて、めっき槽に鉄イオ
ンを供給するために鉄チップを充填した鉄チップ溶解槽
の下方からめっき液を圧入して鉄チップを溶解する場合
に、鉄チップ溶解槽内の円筒軟鉄チップ充填層の径a 
(mm)と高さb (mm)との関係がb/a≦ 3を
満たし、かつ、鉄チップ溶解槽入側のめっき液中のFe
3+濃度を5g/l以上、鉄チップ溶解槽中の鉄チップ
と圧入するめっき液との相対流速を3m/min以上と
し、鉄チップ溶解槽中の鉄チップの溶解中に鉄チップ溶
解槽下部から鉄チップを抜き取って鉄チップ充填層を移
動させることを特徴とする鉄系合金電気めっきにおける
鉄イオン供給方法を第2の発明とする2つの発明よりな
るものである。
Means for Solving Problem E] The method for supplying iron ions in iron-based alloy electroplating according to the present invention includes: (1) In iron-based alloy electroplating, filling a plating bath with iron chips to supply iron ions; When melting iron chips by pressurizing plating solution from below into the iron chip dissolving tank, the diameter a of the cylindrical soft iron chip packed bed in the iron chip dissolving tank is
The relationship between (mm) and height b (IIIll) is b /
a≦3, the p e3 + concentration in the plating solution on the inlet side of the iron chip dissolution tank is 5 g/l or more, and the relative flow rate between the iron chips in the iron chip dissolution tank and the plating solution press-fitted is 3 m
The first invention provides a method for supplying iron ions in electroplating of iron-based alloys, characterized in that the iron ions are supplied to the plating bath in order to supply iron ions to the plating bath in electroplating of iron-based alloys. When melting iron chips by pressurizing plating solution from below into a filled iron chip dissolving tank, the diameter a of the cylindrical soft iron chip filling bed in the iron chip dissolving tank is
(mm) and height b (mm) satisfies b/a≦3, and the Fe content in the plating solution at the entrance side of the iron chip dissolution tank is
3+ concentration is 5 g/l or more, the relative flow velocity between the iron chips in the iron chip dissolving tank and the plating solution press-in is 3 m/min or more, and while the iron chips are melting in the iron chip dissolving tank, from the bottom of the iron chip dissolving tank This invention consists of two inventions, the second invention being a method for supplying iron ions in iron-based alloy electroplating, which is characterized by removing iron chips and moving an iron chip packed bed.

本発明に係る鉄系合金電気めっきにおける鉄イオン供給
方法について、以下詳細に説明する。
The method for supplying iron ions in iron-based alloy electroplating according to the present invention will be described in detail below.

鉄系合金電気めっき槽に鉄イオンを供給する場合に、鉄
チップ溶解槽内に鉄チップを充填し、溶解槽の下部から
めっき液をポンプにより圧入して鉄チップ充填層を通過
させることにより、鉄チップを溶解しめっき槽に送るの
である。
When supplying iron ions to an iron-based alloy electroplating tank, the iron chip dissolution tank is filled with iron chips, and the plating solution is pumped from the bottom of the dissolution tank and passed through the iron chip filling layer. The iron chips are melted and sent to a plating tank.

この場合、鉄の溶解反応としては、 P e+ 2 F e”−+ 3 F e”(F e3
+還元溶解反応)Fe+H” −+Pe” +Ht(水
素発生溶解反応)がある。
In this case, the iron dissolution reaction is P e+ 2 Fe"-+ 3 Fe" (F e3
+Reduction and dissolution reaction)Fe+H''-+Pe'' +Ht (Hydrogen generation and dissolution reaction).

そして、Fe’+イオン還元溶解反応の方が優先的に生
じるために、鉄チップ溶解量はFe3+イオン濃度に大
きく依存する。
Since the Fe'+ ion reduction and dissolution reaction occurs preferentially, the amount of iron chip dissolution largely depends on the Fe3+ ion concentration.

第1図は鉄チップ溶解槽入側のFe3+イオン濃度と鉄
チップ溶解量との関係を示してあり、鉄チップ溶解量は
Fe’+イオン濃度が高い程多くなる。
FIG. 1 shows the relationship between the Fe3+ ion concentration at the entrance side of the iron chip dissolution tank and the amount of iron chips dissolved, and the higher the Fe'+ ion concentration, the greater the amount of iron chips dissolved.

従って、鉄チップ溶解量を多くするためには、鉄チップ
溶解槽入側のFe3+イオン濃度は5g/l以上としな
ければならないことはこの第1図より明らかである。第
1図においては、鉄チップ充填量は500kg、鉄チッ
プとめっき液との相対流速は10m/l1inである。
Therefore, it is clear from FIG. 1 that in order to increase the amount of iron chips dissolved, the Fe3+ ion concentration at the entrance side of the iron chip dissolution tank must be 5 g/l or more. In FIG. 1, the amount of iron chips filled is 500 kg, and the relative flow velocity between the iron chips and the plating solution is 10 m/l1in.

次に、Fe 3 +イオン還元効率におよぼす溶解条件
を調査した結果、F e”イオン濃度の影響が大きいこ
とが判明した。即ち、P e”イオン濃度が低下すると
水素発生溶解反応が多(なってFe3還元効率が低くな
る。特に、めっき液が鉄チップ充填層を通過する場合、
Fe3+イオン還元溶解反応が生じるため、鉄チップ充
填層の入側部から出側部にかけてFe3寸イオン濃度が
徐々に低下するようになる。従って、鉄チップ充填層の
出側部におけるFe3+イオン還元効率が相当低くなり
、入側部から出側部にかけての全Fe3+イオン還元効
率は低下する。この場合、鉄チップ充填層が高くなる程
、このような傾向は顕著となるものと考えられる。
Next, as a result of investigating the dissolution conditions that affect the Fe 3 + ion reduction efficiency, it was found that the Fe" ion concentration has a large influence. In other words, when the P e" ion concentration decreases, the hydrogen generation dissolution reaction increases. In particular, when the plating solution passes through an iron chip packed bed, the Fe3 reduction efficiency becomes low.
Since the Fe3+ ion reduction and dissolution reaction occurs, the Fe3+ ion concentration gradually decreases from the inlet side to the outlet side of the iron chip packed bed. Therefore, the Fe3+ ion reduction efficiency at the outlet side of the iron chip packed bed becomes considerably low, and the total Fe3+ ion reduction efficiency from the inlet side to the outlet side decreases. In this case, it is thought that such a tendency becomes more remarkable as the iron chip filling layer becomes higher.

第2図に鉄チップ充填層の高さ/鉄充填層の径とF e
3Yオン還元効率との関係を示してあり、鉄チップ充填
層の高さ/鉄チップ充填層の径の比率が3を越えるとF
e3+イオン還元効率が著しく低下する。従って、Fe
3+イオン還元効率を高くするためには、鉄チップ充填
層の高さ/鉄チップ充填層の径の比率は3以下としなけ
ればならないことは第2図から明らかである。第2図に
おいて、鉄チップ溶解槽入側のFe3+イオン濃度は8
g/l、鉄チップ充填層の径は400問φである。
Figure 2 shows the height of the iron chip packed bed/diameter of the iron packed bed and F e
It shows the relationship with 3Y-on reduction efficiency, and when the ratio of height of iron chip packed bed/diameter of iron chip packed bed exceeds 3, F
The e3+ ion reduction efficiency is significantly reduced. Therefore, Fe
It is clear from FIG. 2 that in order to increase the 3+ ion reduction efficiency, the ratio of the height of the iron chip packed bed/the diameter of the iron chip packed bed must be 3 or less. In Figure 2, the Fe3+ ion concentration at the entrance side of the iron chip melting tank is 8.
g/l, and the diameter of the iron chip packed bed is 400mmφ.

さらに、鉄チップ溶解槽内における鉄チップに対する鉄
チップを溶解するためのめっき液の相対流速は、:3+
/ll1n以上とする必要があり、3ffl/win未
満では鉄の溶解反応のにより生成した水素ガスが鉄チッ
プの表面に付着したまま脱離しないために、Fe3+イ
オンの鉄チップ表面への拡散が阻害され、Fe’+イオ
ン還元効率および鉄チップ溶解量が共に低くなる。
Furthermore, the relative flow rate of the plating solution for dissolving the iron chips in the iron chip dissolution tank is: 3+
/ll1n or more, and if it is less than 3ffl/win, the hydrogen gas generated by the iron dissolution reaction remains attached to the surface of the iron chip and does not desorb, which inhibits the diffusion of Fe3+ ions to the surface of the iron chip. As a result, both Fe'+ ion reduction efficiency and iron chip dissolution amount become low.

本発明に係る鉄系合金電気めっきにおける鉄イオン供給
方法を実施するための装置について第3図により説明す
る。
An apparatus for carrying out the method for supplying iron ions in iron-based alloy electroplating according to the present invention will be explained with reference to FIG.

鉄チップホッパー2より鉄チップTを鉄チップ溶解槽l
に充填する。次いで、鉄チップTを溶解するためのめっ
き液Mをポンプ(図示せず。)によりめっき液M供給口
12より圧入し、めっき液Mオーバーフロー口Itから
排出させて循環使用することにより鉄チップTを溶解す
る。
Iron chips T are transferred from iron chip hopper 2 to iron chip melting tank L.
Fill it. Next, a plating solution M for dissolving the iron chips T is forced into the plating solution M supply port 12 using a pump (not shown), and is discharged from the plating solution M overflow port It for circulation use. dissolve.

さらに、電動機7および減速機6によりスクリュウロッ
ド8を回転させてスクリュウにより鉄チップ溶解槽1の
下部より、溶解して微細化した鉄チップを抜き取りスラ
ッジバッグ9に受けるようにする。
Further, the screw rod 8 is rotated by the electric motor 7 and the speed reducer 6, and the iron chips which have been melted and made into fine particles are extracted from the lower part of the iron chip melting tank 1 by the screw and received in the sludge bag 9.

このように、鉄チップ溶解槽の下部から鉄チップを抜き
取ることにより、鉄チップ充填層を下方に移動させる。
In this way, by extracting the iron chips from the lower part of the iron chip dissolving tank, the iron chip packed bed is moved downward.

従って、溶解により微細化した鉄チップが取り除かれ、
鉄チップ充填層内の横断面における鉄チップ粒度が均一
となるため、銖チッブを溶解するための圧入されためっ
き液の偏流がなくなる。また、鉄チップが移動するため
鉄チップに付着している水素ガスが容易に脱離される。
Therefore, fine iron chips are removed by melting,
Since the iron chip particle size in the cross section in the iron chip packed bed becomes uniform, there is no uneven flow of the plating solution press-ined to dissolve the iron chips. Furthermore, since the iron chip moves, hydrogen gas adhering to the iron chip is easily desorbed.

従って、鉄チップ溶解量が安定化し、Fe3+イオンの
還元効率を向上させることができる。なお、鉄系合金電
気めっき液は硫酸浴であり、p)(はO〜3、浴温度4
0〜80℃とする。
Therefore, the amount of dissolved iron chips is stabilized, and the reduction efficiency of Fe3+ ions can be improved. Note that the iron-based alloy electroplating solution is a sulfuric acid bath, p) (is O ~ 3, bath temperature 4
The temperature shall be 0 to 80°C.

鉄チップの形状は、粒状、板状、線状、塊状等の何れで
もよく、大きさは特に限定的ではないが、めっき液と鉄
チップの相対流速が容易に得られ易い点から、直径がl
nmφnm上するのが望ましく、また、溶解速度の点か
らは比表面積の大きなものが必要であり、直径110l
l1φ以下のものが望ましい。
The shape of the iron chip may be granular, plate-like, linear, block-like, etc., and the size is not particularly limited, but from the viewpoint of easily obtaining the relative flow rate between the plating solution and the iron chip, the diameter is l
It is desirable to have a diameter of 110 l.
It is desirable that the diameter be less than l1φ.

[実 施 例] 本発明に係る鉄系合金電気めっきにおける鉄イオン供給
方性の実施例を説明する。
[Example] An example of iron ion supply direction in iron-based alloy electroplating according to the present invention will be described.

実施例 直径400mmの鉄チップ溶解槽筒体内に平均粒径3a
+mの鉄チップ450〜600kgを充填し、鉄チップ
溶解のためのめつき液と鉄チップの相対流速3m、/+
in、6m/min、  10m/winとして、めっ
き液を循環させた。
Example: Iron chip melting tank cylinder with a diameter of 400 mm contained an average particle size of 3a.
Filled with 450 to 600 kg of iron chips of + m, relative flow rate of plating liquid for dissolving iron chips and iron chips of 3 m, /+
The plating solution was circulated at a rate of 6 m/min, 10 m/win.

めっき液組成 F eS OF2 HtO:  350g/ lZn5
O−・7HtO:   I Og/IH1SO,:  
 10g/l pe”           :   6g/l、 8
g/l、10g/l 浴温   60℃ 実施例No、1〜N004は鉄チップ充填層は固定して
おり、実施例No、5〜8は鉄チップ充填層の下部から
鉄チップを抜き取った場合である(本発明に係る鉄系合
金電気めっきにおける鉄イオン供給方性。)。
Plating solution composition FeS OF2 HtO: 350g/lZn5
O-・7HtO: I Og/IH1SO,:
10g/l pe”: 6g/l, 8
g/l, 10 g/l Bath temperature 60°C In Examples No. 1 to No. 004, the iron chip packed bed is fixed, and in Example Nos. 5 to 8, the iron chips are extracted from the bottom of the iron chip packed bed. (Iron ion supply direction in iron-based alloy electroplating according to the present invention.)

実施例No、9〜No、 12は鉄チップ充填層は固定
しており、実施例No、 13は鉄チップ充填層の下部
から鉄チップを抜き取った場合である(比較例。)。
In Examples No. 9 to No. 12, the iron chip filling layer is fixed, and in Example No. 13, the iron chips are extracted from the lower part of the iron chip filling layer (comparative examples).

第1表に溶解条件およびその結果を示す。Table 1 shows the dissolution conditions and results.

Fe3還元効率および鉄チップ溶解量は鉄チップ溶解槽
入側、出側のめっき液を採取し、Fe’濃度とH,SO
,濃度の変動量から次式により算出した。
Fe3 reduction efficiency and iron chip dissolution amount were determined by collecting the plating solution at the entrance and exit of the iron chip dissolution tank, and measuring the Fe' concentration and H,SO
, was calculated from the amount of variation in concentration using the following formula.

Fe3+還元効率=(△F e” (+nol/ 1)
)/ (△Fe”(mol/I)+ 2 x△)(ts
o4(mol/l))X 100(%)鉄溶解量=(△
F e”(kg/Hr))/ (2x F e”還元効
率)x 100 (kg/Hr) [発明の効果] 以上詳細に説明したように、本発明に係る鉄系合金電気
めっきにおける鉄イオン供給方法は上記の横絞であるか
ら、鉄系合金電気めっきのめっき槽に鉄イオンを供給す
るに際して、鉄チップ溶解槽中の鉄チップの溶解量を常
に安定させることができ、そして、Fe’+還元効率を
著しく向上させることができ、さらに、長時間にわたり
安定した操業を行なうことができるという優れた効果を
有するものである。
Fe3 + reduction efficiency = (△F e” (+nol/ 1)
)/(△Fe”(mol/I)+2 x△)(ts
o4 (mol/l))X 100(%) Iron dissolution amount = (△
Fe" (kg/Hr))/(2x Fe" reduction efficiency) x 100 (kg/Hr) [Effects of the invention] As explained in detail above, iron ions in the iron-based alloy electroplating according to the present invention Since the supply method is the above-mentioned horizontal throttling, when supplying iron ions to the plating tank for iron-based alloy electroplating, the amount of iron chips dissolved in the iron chip dissolution tank can always be stabilized, and Fe' + It has the excellent effect of being able to significantly improve the reduction efficiency and also being able to operate stably over a long period of time.

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

第1図は鉄チップ溶解槽人側のFe3+イオン濃度と鉄
チップ溶解量との関係を示す図、第2図は鉄チップ充填
層の高さ/鉄チップ充填層の径の比とp e3 +イオ
ン還元効率との関係を示す図、第3図は本発明に係る鉄
系合金電気めっきにおける鉄イオン供給方法を実施する
ための装置の例を示す図である。 夏〜鉄チップ溶解槽、2〜鉄チツプホツパー3〜バルブ
、4〜ガス抜き孔、5〜窒素/空気供給孔、6〜減速機
、7〜電動機、8〜スクリユウロツド、9〜スラツジ受
バツグ、XO〜多孔板、11〜オーバーフローロ、12
めっき液供給口。
Figure 1 shows the relationship between the Fe3+ ion concentration on the user side of the iron chip dissolution tank and the amount of iron chip dissolution, and Figure 2 shows the relationship between the height of the iron chip packed bed/diameter of the iron chip packed bed and p e3 + A diagram showing the relationship with ion reduction efficiency, and FIG. 3 is a diagram showing an example of an apparatus for carrying out the iron ion supply method in iron-based alloy electroplating according to the present invention. Summer ~ iron chip melting tank, 2 ~ iron chip hopper 3 ~ valve, 4 ~ gas vent hole, 5 ~ nitrogen/air supply hole, 6 ~ speed reducer, 7 ~ electric motor, 8 ~ screw rod, 9 ~ sludge receiving bag, XO ~ Perforated plate, 11 ~ Overflow, 12
Plating solution supply port.

Claims (2)

【特許請求の範囲】[Claims] (1)鉄系合金電気めっきにおいて、めっき槽に鉄イオ
ンを供給するために鉄チップを充填した鉄チップ溶解槽
の下方からめっき液を圧入して鉄チップを溶解する場合
に、鉄チップ溶解槽内の円筒状鉄チップ充填層の径a(
mm)と高さb(mm)との関係がb/a≦3を満たし
、かつ、鉄チップ溶解槽入側のめっき液中のFe^3^
+濃度を5g/l以上、鉄チップ溶解槽中の鉄チップと
圧入するめっき液との相対流速を3m/min以上とす
ることを特徴とする鉄系合金電気めっきにおける鉄イオ
ン供給方法。
(1) In iron-based alloy electroplating, when dissolving iron chips by pressurizing the plating solution from below into the iron chip dissolving tank filled with iron chips in order to supply iron ions to the plating tank, the iron chip dissolving tank is used. The diameter a of the cylindrical iron chip packed bed inside (
The relationship between the height b (mm) and the height b (mm) satisfies b/a≦3, and the Fe^3^ in the plating solution on the entrance side of the iron chip dissolution tank
+ A method for supplying iron ions in iron-based alloy electroplating, characterized in that the concentration is 5 g/l or more, and the relative flow velocity between the iron chips in the iron chip dissolving tank and the plating solution press-in is 3 m/min or more.
(2)鉄系合金電気めっきにおいて、めっき槽に鉄イオ
ンを供給するために鉄チップを充填した鉄チップ溶解槽
の下方からめっき液を圧入して鉄チップを溶解する場合
に、鉄チップ溶解槽内の円筒状鉄チップ充填層の径a(
mm)と高さb(mm)との関係がb/a≦3を満たし
、かつ、鉄チップ溶解槽入側のめっき液中のFe^3^
+濃度を5g/l以上、鉄チップ溶解槽中の鉄チップと
圧入するめっき液との相対流速を3m/min以上とし
、鉄チップ溶解槽中の鉄チップの溶解中に鉄チップ溶解
槽下部から鉄チップを抜き取って鉄チップ充填層を移動
させることを特徴とする鉄系合金電気めっきにおける鉄
イオン供給方法。
(2) In iron-based alloy electroplating, when dissolving iron chips by pressurizing the plating solution from below into the iron chip dissolving tank filled with iron chips in order to supply iron ions to the plating tank, the iron chip dissolving tank is used. The diameter a of the cylindrical iron chip packed bed inside (
The relationship between the height b (mm) and the height b (mm) satisfies b/a≦3, and the Fe^3^ in the plating solution on the entrance side of the iron chip dissolution tank
+ The concentration is 5 g/l or more, the relative flow velocity between the iron chips in the iron chip dissolving tank and the plating solution press-in is 3 m/min or more, and while the iron chips are melting in the iron chip dissolving tank, from the bottom of the iron chip dissolving tank A method for supplying iron ions in iron-based alloy electroplating, characterized by extracting iron chips and moving an iron chip packed layer.
JP3881690A 1990-02-20 1990-02-20 Supplying method for iron ion in electroplating iron-based alloy Pending JPH03243798A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3881690A JPH03243798A (en) 1990-02-20 1990-02-20 Supplying method for iron ion in electroplating iron-based alloy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3881690A JPH03243798A (en) 1990-02-20 1990-02-20 Supplying method for iron ion in electroplating iron-based alloy

Publications (1)

Publication Number Publication Date
JPH03243798A true JPH03243798A (en) 1991-10-30

Family

ID=12535794

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3881690A Pending JPH03243798A (en) 1990-02-20 1990-02-20 Supplying method for iron ion in electroplating iron-based alloy

Country Status (1)

Country Link
JP (1) JPH03243798A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20240151189A (en) 2022-03-18 2024-10-17 제이에프이 스틸 가부시키가이샤 Method for circulating iron-based electroplating solution, method for producing iron-based electroplating solution, and method for producing alloyed hot-dip galvanized steel sheet

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20240151189A (en) 2022-03-18 2024-10-17 제이에프이 스틸 가부시키가이샤 Method for circulating iron-based electroplating solution, method for producing iron-based electroplating solution, and method for producing alloyed hot-dip galvanized steel sheet
EP4729668A2 (en) 2022-03-18 2026-04-22 JFE Steel Corporation Method for circulating iron-based electroplating solution
EP4729667A2 (en) 2022-03-18 2026-04-22 JFE Steel Corporation Method for manufacturing iron-based electroplating solution and method for manufacturing alloyed hot-dip galvanized steel sheet

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