JPH08193300A - Method for separating and recovering undissolved metal - Google Patents

Method for separating and recovering undissolved metal

Info

Publication number
JPH08193300A
JPH08193300A JP7004804A JP480495A JPH08193300A JP H08193300 A JPH08193300 A JP H08193300A JP 7004804 A JP7004804 A JP 7004804A JP 480495 A JP480495 A JP 480495A JP H08193300 A JPH08193300 A JP H08193300A
Authority
JP
Japan
Prior art keywords
trough
plating solution
undissolved
plating
separating
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.)
Withdrawn
Application number
JP7004804A
Other languages
Japanese (ja)
Inventor
Ichirou Tanoguchi
一郎 田野口
Takao Ikenaga
孝雄 池永
Osamu Shin
修 進
Shiyuuji Kaeriyama
周士 帰山
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 JP7004804A priority Critical patent/JPH08193300A/en
Publication of JPH08193300A publication Critical patent/JPH08193300A/en
Withdrawn legal-status Critical Current

Links

Abstract

PURPOSE: To propose a method for easily separating and recovering a large amt. of undissolved metal powder difficult to separate with a generally used filter-cloth filter due to clogging. CONSTITUTION: A ferromagnetic powder is dissolved in an acidic soln. in a dissolution tank 1 to produce a plating soln. 5 which is transported to a plating bath 5 from the tank 1, and the undissolved magnetic powder is separated and recovered with a magnet 6 in the intervening passage. In this case, a freely tiltable trough 2 is formed in the plating soln. passage, the magnet 6 capable of being magnetically turned on and off is furnished to the bottom face of the trough, the magnetic force-impressed trough 2 is tilted toward the downstream side to pass the plating soln. 5, hence the undissolved metal is deposited on the trough bottom, the trough 2 is tilted toward the dissolution tank 1, the magnetic force is turned off, and the deposit is dropped into the dissolution tank.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、めっき液の製造方法に
関し、詳しくは、Fe、Ni等の強磁性金属粉を酸液へ
溶解してめっき液を製造する工程において、溶解槽内で
溶解後にめっっき浴へ搬送途中で、未溶解の上記金属粉
をめっき液から分離、回収する方法に係わる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a plating solution, and more specifically, in a step of producing a plating solution by dissolving ferromagnetic metal powder such as Fe or Ni in an acid solution, the solution is dissolved in a dissolution tank. The present invention relates to a method of separating and recovering the undissolved metal powder from the plating solution during transportation to the plating bath later.

【0002】[0002]

【従来の技術】めっき鋼板の製造においては、めっき液
を新しく製造したり、めっき実施によるめっき金属の消
費を補給するため、めっき金属を酸液等で溶解する必要
がある。その溶解作業は、溶解槽内にめっき金属粉と酸
液又は使用済のめっき液を装入し、両者を接触、溶解
し、そこで生成しためっき液をめっき浴へ供給するのが
一般的である。そして、かかる溶解作業で重要なこと
は、めっき液中へ未溶解の金属粉が混入し、めっき鋼板
の疵発生の原因とならないようにすることである。その
ため、未溶解金属粉の分離、回収あるいはその再溶解に
関しては、従来より多くの研究開発がなされ、主として
濾布フィルタを用いるプレスフィルタ、リーフフィルタ
を有効に活用した技術が知られ、盛んに利用されてい
る。このフィルタ方式の分離回収の1例に、特公昭62
−10684号公報は「難溶性被溶解物を懸濁させた液
をフィルタを介して、タンクに供給し、該タンクの溶液
を使用する方法において、溶液の一部を前記タンクから
フィルタに循環して難溶性物質を溶解する」技術を開示
している。
2. Description of the Related Art In the production of plated steel sheets, it is necessary to dissolve the plating metal with an acid solution or the like in order to newly produce the plating solution or to supplement the consumption of the plating metal due to the plating. In the melting operation, it is common to load the plating metal powder and the acid solution or the used plating solution into a melting tank, contact and melt both, and supply the plating solution produced there to the plating bath. . What is important in such melting work is to prevent unmelted metal powder from being mixed into the plating solution and causing defects in the plated steel sheet. For this reason, much research and development has been conducted on the separation, recovery, or re-dissolution of undissolved metal powder, and techniques that effectively utilize press filters and leaf filters that mainly use filter cloth filters are known and are actively used. Has been done. One example of this filter-based separation and collection is
No. 10684, “In a method of supplying a liquid in which a hardly soluble substance is suspended to a tank through a filter and using a solution in the tank, a part of the solution is circulated from the tank to the filter. "Dissolves a poorly soluble substance".

【0003】一方、めっき金属がFe,Ni等の強磁性
体である場合には、当然に磁石の利用が考えられ、例え
ば実公平3−18511号公報は、めっき液を下方から
上方へ送る方式の溶解槽の上端部周囲にオーバーフロー
液を受けるめっき液樋を設け、その樋内周に磁石を、外
周に捕集網を樋全面に設けた電気めっき液への鉄イオン
補給装置を開示した。また、実開昭62−198273
号公報は、上記溶解槽のオーバフロー液を受ける液樋に
磁石を設けることに換え、オーバフロー液をめっきライ
ンへ送る供給管の中に磁気フィルタを配置し、未溶解鉄
粒を分離、回収する装置を開示している。さらに、特開
昭50−60868号公報は、水路底面に複数個電磁石
を設置し、一定方向に順次磁化させることにより磁性体
を一定方向に移動させ、集められたものを回収して水溶
液と分離する方法を、あるいは特開昭51−61073
号公報は、水溶液を保持している容器に外部から磁界を
加え、磁界を逐次排出口に向かって移動させることによ
り、磁性粒子を該排出口に集めてここから外部に排出す
る方法を提案している。
On the other hand, when the plating metal is a ferromagnetic material such as Fe or Ni, it is naturally conceivable to use a magnet. For example, Japanese Utility Model Publication No. 3-18511 discloses a method in which the plating solution is sent from the bottom to the top. Disclosed is an iron ion replenishing device for an electroplating solution in which a plating solution trough for receiving an overflow solution is provided around the upper end of the melting tank, a magnet is provided on the inner circumference of the trough, and a collecting net is provided on the outer circumference of the trough. In addition, the actual exploitation Sho 62-198273
The publication discloses a device for separating and recovering undissolved iron particles by disposing a magnet in a liquid gutter that receives the overflow liquid in the above-mentioned dissolution tank, and by disposing a magnetic filter in a supply pipe that sends the overflow liquid to a plating line. Is disclosed. Further, JP-A-50-60868 discloses that a plurality of electromagnets are installed on the bottom surface of a water channel and sequentially magnetized in a certain direction to move a magnetic body in a certain direction, and the collected matter is collected and separated from an aqueous solution. Or the method described in JP-A-51-61073.
The publication proposes a method of applying a magnetic field from the outside to a container holding an aqueous solution and sequentially moving the magnetic field toward the discharge port to collect the magnetic particles at the discharge port and discharge the magnetic particles to the outside. ing.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、特公昭
62−10684号公報記載のような濾布フィルタを用
いる技術は、未溶解粉体の量が非常に多い場合、濾布フ
ィルタを通過する水溶液流量が目詰りにより極めて小さ
くなるため、非常に大きな濾布面積が必要となり、大き
な設備となるばかりでなく、逆洗作業や濾布交換作業が
頻繁に必要で作業性が悪いという問題点がある。また、
磁石を利用する技術も、特開昭50−60868号公報
記載のものは、一定の場所に磁性体を集めるだけである
ため、集めた磁性体を液中から取り出す作業が別途必要
になり、分離回収のための有効な手段としては今一歩で
ある。さらに、特開昭51−61073号公報記載の技
術は、排出口から磁性粒子のみを排出し、水溶液を出さ
ずにシールすることは実質的に不可能である。つまり、
磁性粒子が一定量溜っている定常状態の場合には、該排
出口からの水溶液の流出防止はできるが、最初に水溶液
を該容器に通液した当初では、磁性粒子がある程度溜る
まで全ての水溶液が流出してしまうという欠点がある。
加えて、粒径数μm以下の超微粒子を分離する手段とし
て、本出願人が先に特願平6−233194号で出願し
た中空フィルタも知られているが、未溶解粉体の量が多
い場合、前記特公昭62−10684号と同様、フィル
タの目詰りにより使用不可となることが多く、溶解作業
の中断をしなければならないという問題があった。な
お、該中空フィルタは、多孔質セラミックス体からな
り、例えば図3に示すような形状のものや、所謂中空系
フィルタを用いれば良い。
However, the technique of using a filter cloth filter as described in Japanese Patent Publication No. 62-10684 has a problem in that when the amount of undissolved powder is very large, the flow rate of the aqueous solution passing through the filter cloth filter is large. Since it becomes extremely small due to clogging, a very large filter cloth area is required, and not only a large facility is required, but also backwashing work and filter cloth replacement work are frequently required, resulting in poor workability. Also,
In the technology utilizing a magnet, the one disclosed in Japanese Patent Laid-Open No. 50-60868 only collects the magnetic substance at a certain place, and therefore, the work of taking out the collected magnetic substance from the liquid is separately required, and the separation is performed. It is just one step away as an effective means of recovery. Further, in the technique described in Japanese Patent Laid-Open No. 51-61073, it is substantially impossible to discharge only the magnetic particles from the discharge port and to seal without discharging the aqueous solution. That is,
In a steady state in which a certain amount of magnetic particles are accumulated, it is possible to prevent the aqueous solution from flowing out from the outlet, but at the beginning when the aqueous solution is first passed through the container, all the aqueous solution is retained until the magnetic particles are accumulated to some extent. Has the drawback of being leaked.
In addition, as a means for separating ultrafine particles having a particle size of several μm or less, a hollow filter previously filed by the present applicant in Japanese Patent Application No. 6-233194 is also known, but the amount of undissolved powder is large. In this case, as in Japanese Patent Publication No. 62-10684, the filter is often unusable, and there is a problem that the melting operation must be interrupted. The hollow filter is made of a porous ceramics body, and for example, one having a shape as shown in FIG. 3 or a so-called hollow filter may be used.

【0005】そこで、本発明は、かかる事情を鑑み、未
溶解の金属粉の量が非常に多く、一般に用いられる濾布
方式のフィルタでは濾布の目詰りにより分離困難な場合
であっても、多量の未溶解金属粉を磁力によって容易に
分離回収できる方法を提案することを目的としている。
In view of the above situation, the present invention has a very large amount of undissolved metal powder, and even if a commonly used filter cloth type filter is difficult to separate due to clogging of the filter cloth, The purpose is to propose a method that can easily separate and collect a large amount of undissolved metal powder by magnetic force.

【0006】[0006]

【課題を解決するための手段】発明者は、上記目的を達
成するため、溶解槽内の未溶解金属粉を含む液を底面に
電磁石又は永久磁石を設置した樋流路へ導き、金属粉を
磁石により樋底面に吸着させ、液のみを流出させるに際
して、磁力のON/OFF操作と上記樋の傾きとを組合
わせることに着眼し、鋭意検討を行った。本発明は、そ
の検討成果を具現化したものである。すなわち、本発明
は、強磁性金属粉を溶解槽中で酸液に溶解してめっき液
を製造し、該めっき液を該溶解槽からめっき浴に搬送す
る途中の流路で該めっき液から該強磁性金属粉の未溶解
分を磁石によって分離回収する方法において、上記めっ
き液流路に傾動自在の傾注樋を設けると共に、該樋底面
に磁力のON/OFFが可能な磁石を配設し、磁力を印
加した該傾注樋をその下流側に傾けめっき液を通過させ
ることにより未溶解金属を樋底部に付着させ、該傾注樋
を溶解槽側に傾け磁力を切ることにより該付着物を該溶
解槽に落し込むことを特徴とする未溶解金属の分離回収
方法である。また、本発明は、上記傾注樋をその下流側
に傾けてめっき浴の方向へ通過させためっき液を、さら
に中空フィルタを通過させることを特徴とする未溶解金
属の分離回収方法である。さらに、本発明は、上記傾注
樋の傾き方向の変更をその上を通過させためっき液の累
積流量に基づき自動的に行うことを特徴とする未溶解金
属の分離回収方法でもある。
Means for Solving the Problems In order to achieve the above object, the inventor introduces a liquid containing undissolved metal powder in a melting tank into a gutter flow path having an electromagnet or a permanent magnet installed on the bottom surface to remove the metal powder. When adsorbing only the liquid on the bottom of the trough with a magnet and letting out only the liquid, attention was paid to the combination of the ON / OFF operation of the magnetic force and the inclination of the above-mentioned trough, and earnestly studied. The present invention embodies the results of the study. That is, the present invention is to prepare a plating solution by dissolving ferromagnetic metal powder in an acid solution in a dissolution tank, and to remove the plating solution from the plating solution in a flow path on the way of transporting the plating solution from the dissolution tank to a plating bath. In the method of separating and recovering the undissolved portion of the ferromagnetic metal powder with a magnet, a tilting gutter that can be tilted is provided in the plating solution flow path, and a magnet that can turn on / off the magnetic force is provided on the bottom surface of the gutter. The undissolved metal is adhered to the trough bottom by tilting the tilted trough to which magnetic force is applied to the downstream side and passing the plating solution, and tilting the tilted trough to the melting tank side to cut off the magnetic force to melt the deposit. It is a method for separating and recovering undissolved metal, which is characterized by dropping into a tank. The present invention is also a method for separating and recovering undissolved metal, characterized in that the above-mentioned slanted trough is tilted to the downstream side and passed through in the direction of the plating bath, and further passed through a hollow filter. Furthermore, the present invention is also a method for separating and recovering undissolved metal, characterized in that the inclination direction of the tilting gutter is automatically changed based on the cumulative flow rate of the plating solution passed therethrough.

【0007】[0007]

【作用】本発明では、強磁性金属粉を溶解槽中で酸液に
溶解してめっき液を製造し、該めっき液を該溶解槽から
めっき浴に搬送する途中の流路で該めっき液から該強磁
性金属粉の未溶解分を磁石によって分離回収する方法に
おいて、上記めっき液流路に傾動自在の傾注樋を設ける
と共に、該樋底面に磁力のON/OFFが可能な磁石を
配設し、磁力を印加した該傾注樋をその下流側に傾けめ
っき液を通過させることにより未溶解金属を樋底部に付
着させ、該傾注樋を溶解槽側に傾け磁力を切ることによ
り該付着物を該溶解槽に落し込むようにしたので、未溶
解金属量が多くても、濾布式フィルタを用いる場合のよ
うに、フィルタの目詰りを懸念する必要はなく円滑に分
離、回収ができるようになる。その結果、溶解作業の中
断は皆無になり、めっき作業が安定して行えるようにな
った。
In the present invention, a ferromagnetic metal powder is dissolved in an acid solution in a dissolution tank to produce a plating solution, and the plating solution is removed from the plating solution in a flow path in the course of being conveyed from the dissolution tank to a plating bath. In the method of separating and recovering the undissolved portion of the ferromagnetic metal powder with a magnet, a tilting gutter that can be tilted is provided in the plating solution flow path, and a magnet that can turn on / off the magnetic force is provided on the bottom surface of the gutter. , The undissolved metal is adhered to the trough bottom by tilting the tilted trough to which magnetic force is applied to the downstream side of the plating solution, and the tilted trough is tilted toward the melting tank to cut off the magnetic force. Since it was dropped into the melting tank, even if there is a large amount of undissolved metal, there is no need to worry about clogging of the filter as in the case of using a filter cloth type filter, and separation and collection can be done smoothly. . As a result, there was no interruption of melting work, and plating work became stable.

【0008】また、本発明では、上記傾注樋をその下流
側に傾けてめっき浴の方向へ通過させためっき液を、さ
らに中空フィルタを通過させるようにしたので、未溶解
金属粉末が微粒子でも回収できるようになり、生成した
めっき液にそれが残り、めっきの品質を悪化させること
もなくなる。さらに、本発明では、上記傾注樋の傾き方
向の変更をその上を通過させためっき液の累積流量に基
づき自動的に行うようにしたので、溶解作業が人手を介
さずに円滑に行われるようになり、作業効率の向上、省
力化が図れた。
Further, in the present invention, the undiluted metal powder is recovered even in the form of fine particles, because the plating solution obtained by inclining the inclined trough toward the downstream side thereof and passing it in the direction of the plating bath is further passed through the hollow filter. As a result, it remains in the generated plating solution and does not deteriorate the quality of plating. Further, in the present invention, the tilt direction of the tilt gutter is automatically changed based on the cumulative flow rate of the plating solution passed therethrough, so that the melting operation can be smoothly performed without human intervention. As a result, work efficiency has been improved and labor has been saved.

【0009】以下、実施例において、図1〜2に基づ
き、本発明を具体的に説明する。
In the following, the present invention will be specifically described with reference to FIGS.

【0010】[0010]

【実施例】pHが1.4、温度80℃の硫酸系めっき液
に、平均粒径10μmの金属Ni粉を溶解した。その際
使用した溶解槽の容量は10m3 であり、そこに金属N
i粉を600kg投入し、機械的手段で20分間撹拌し
ながら溶解した。しかし、約500kgの金属Ni粉が
未溶解となり、1μmまで捕集できる濾布フィルタを使
用したがすぐに目詰まりが発生し、効率良く濾過できな
かった。
Example A metallic Ni powder having an average particle diameter of 10 μm was dissolved in a sulfuric acid plating solution having a pH of 1.4 and a temperature of 80 ° C. The capacity of the melting tank used at that time was 10 m 3 , and the metal N
600 kg of i powder was added and dissolved by mechanical means for 20 minutes while stirring. However, about 500 kg of metal Ni powder was undissolved, and a filter cloth filter capable of collecting up to 1 μm was used, but clogging occurred immediately, and efficient filtration was not possible.

【0011】そこで、かかる状態にあるめっき液に本発
明に係る未溶解金属の分離回収方法を適用した。図1
は、その際使用した装置の1慨念図である。まず、未溶
解金属Ni粉を含むめっき液5を、溶解槽1よりポンプ
1 により底部に磁石6を設けた傾注樋2へ一定の流量
で導く。この磁石6は電磁石、永久磁石いずれでもかま
わないが、その磁力は必要に応じてON/OFFできる
ことが重要である。そして、該傾注樋は、磁力がONの
状態の時、その下方に位置するクッションタンク3に該
めっき液5が流入できるよう傾けてある。その結果、め
っき液5中の未溶解金属Ni粉は、磁石に吸着されて該
傾注樋の底部に吸着すると共に、堆積した状態となり、
未溶解粉をほとんど含まないうわずみ液だけがクッショ
ンタンク3へ移行する。
Therefore, the method for separating and recovering undissolved metal according to the present invention was applied to the plating solution in such a state. FIG.
[Fig. 1] is a conceptual diagram of the device used at that time. First, the plating solution 5 containing undissolved metal Ni powder is introduced from the dissolution tank 1 to the tilting trough 2 having a magnet 6 at the bottom by a pump P 1 at a constant flow rate. The magnet 6 may be either an electromagnet or a permanent magnet, but it is important that its magnetic force can be turned ON / OFF as required. The tilting trough is tilted so that the plating solution 5 can flow into the cushion tank 3 located therebelow when the magnetic force is ON. As a result, the undissolved metallic Ni powder in the plating solution 5 is adsorbed by the magnet and adsorbed on the bottom of the tilted gutter, and becomes a deposited state.
Only the soothing liquid containing almost no undissolved powder is transferred to the cushion tank 3.

【0012】次に、上記傾注樋2上へ堆積した未溶解金
属Ni粉の回収方法は、図2で明らかなように、溶解槽
1へ該未溶解金属粉が流入し易いように傾注樋2を傾
け、磁力をOFFとすることで行われる。磁石6が電磁
石では電源をOFFとすれば良く、また永久磁石では樋
底面からの距離を離すことで容易に目的は達成できる。
なお、この場合、溶解に使用する新鮮な(未溶解金属粉
を含まない)酸液で樋を洗い流せば、未溶解金属粉の回
収と溶解槽への新液の注入が同時に行われることも可能
である。また、めっき液の清浄度をあげるためには、図
1に示すように、クッションタンク3の液をポンプP2
により中空フィルタ4に導くことにより、傾注樋2で補
足されなかった微少の未溶解金属粉も分離することが可
能となる。さらに、溶解方法は、バッチ式の場合、図
1、図2の状態を順次繰り返せばよく、連続式の場合
は、複数個の傾注樋を並列に設置しておき、各傾注樋を
通過させるめっき液流量を積算して一定量ごとに、磁力
のON/OFF切替と、傾注樋の角度変更とを行える公
知の手段を付加しておけば良い。
Next, the method of recovering the undissolved metal Ni powder deposited on the above-mentioned slant gutter 2 is, as is clear from FIG. 2, the slant gutter 2 so that the undissolved metal powder easily flows into the dissolution tank 1. It is performed by tilting and turning off the magnetic force. If the magnet 6 is an electromagnet, the power source may be turned off, and if the magnet 6 is a permanent magnet, the object can be easily achieved by separating it from the gutter bottom surface.
In this case, if the gutter is rinsed with a fresh acid solution (not containing undissolved metal powder) used for dissolution, recovery of undissolved metal powder and injection of new solution into the dissolution tank can be performed simultaneously. Is. Further, in order to increase the cleanliness of the plating solution, as shown in FIG. 1, a pump liquid cushion tank 3 P 2
Thus, by guiding the powder to the hollow filter 4, it becomes possible to separate even a minute amount of undissolved metal powder that has not been captured by the inclined trough 2. Further, as for the melting method, in the case of a batch method, the states of FIGS. 1 and 2 may be sequentially repeated, and in the case of a continuous method, a plurality of slant gutters are installed in parallel and plating is performed by passing each slant gutter. It suffices to add a known means capable of integrating the liquid flow rate and switching the magnetic force ON / OFF and changing the angle of the tilting gutter for each fixed amount.

【0013】ちなみに、この金属Ni粉の溶解に、本発
明に係る未溶解金属の分離回収方法を適用した結果を、
クッションタンク3内に溜っためっき液中の未溶解金属
Ni粉含有量で示すと、それは0.1g/リッタ以下で
あった。さらに、該めっき液を粒径0.1μmのまでの
粒子を捕集できる中空フィルタを通すことにより、未溶
解金属Ni粉含有量を皆無とすることができた。
By the way, the results of applying the method for separating and recovering the undissolved metal according to the present invention to the dissolution of the metallic Ni powder are as follows:
The content of undissolved metal Ni powder in the plating solution accumulated in the cushion tank 3 was 0.1 g / liter or less. Furthermore, by passing the plating solution through a hollow filter capable of collecting particles having a particle size of up to 0.1 μm, the content of undissolved metallic Ni powder could be eliminated.

【0014】[0014]

【発明の効果】以上述べたように、本発明により、めっ
き液中に未溶解金属が非常に多く、濾布フィルタでは目
詰りによって分離、回収が困難な場合でも、円滑に該未
溶解金属の分離回収が可能になった。
As described above, according to the present invention, even if the plating solution contains a large amount of undissolved metal and the filter cloth filter is difficult to separate and collect due to clogging, the undissolved metal can be smoothly removed. It became possible to separate and collect.

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

【図1】本発明に係る未溶解金属の分離回収方法を実施
する設備の一例を示す模式図である。
FIG. 1 is a schematic diagram showing an example of equipment for carrying out a method for separating and recovering undissolved metal according to the present invention.

【図2】図1の傾注樋で傾斜角度を変更した状態を示す
図である。
FIG. 2 is a view showing a state in which the tilt angle is changed by the tilt gutter of FIG.

【図3】中空フィルタの形状を示す斜視図である。FIG. 3 is a perspective view showing the shape of a hollow filter.

【符号の説明】[Explanation of symbols]

1 溶解槽 2 傾注樋 3 クッションタンク 4 中空フィルタ 5 めっき液 6 磁石 7 中空部 8 機械的撹拌手段 P1 ポンプ1 P2 ポンプ2DESCRIPTION OF SYMBOLS 1 Dissolution tank 2 Inclined gutter 3 Cushion tank 4 Hollow filter 5 Plating solution 6 Magnet 7 Hollow part 8 Mechanical stirring means P 1 pump 1 P 2 pump 2

───────────────────────────────────────────────────── フロントページの続き (72)発明者 進 修 倉敷市水島川崎通1丁目(番地なし) 川 崎製鉄株式会社水島製鉄所内 (72)発明者 帰山 周士 倉敷市水島川崎通1丁目(番地なし) 川 崎製鉄株式会社水島製鉄所内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Susumu 1-chome, Mizushima Kawasaki-dori, Kurashiki City (no address) Inside the Mizushima Steel Works, Kawasaki Steel Works (72) Inventor Shuji Kayama 1-chome, Mizushima Kawasaki-dori, Kurashiki City None) Inside Kawashima Steel Works Mizushima Steel Works

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 強磁性金属粉を溶解槽中で酸液に溶解し
てめっき液を製造し、該めっき液を該溶解槽からめっき
浴に搬送する途中の流路で、該めっき液より該強磁性金
属粉の未溶解分を磁石によって分離回収する方法におい
て、 上記めっき液流路に傾動自在の傾注樋を設けると共に、
該樋底面に磁力のON/OFFが可能な磁石を配設し、
磁力を印加した該傾注樋をその下流側に傾けめっき液を
通過させることにより未溶解金属を樋底部に付着させ、
該傾注樋を溶解槽側に傾け磁力を切ることにより該付着
物を該溶解槽に落し込むことを特徴とする未溶解金属の
分離回収方法。
1. A ferromagnetic metal powder is dissolved in an acid solution in a dissolution tank to produce a plating solution, and the plating solution is transferred from the dissolution tank to a plating bath in a flow path during which the plating solution is removed from the plating solution. In the method of separating and recovering the undissolved portion of the ferromagnetic metal powder with a magnet, a tilting gutter that can be tilted is provided in the plating solution flow path,
A magnet capable of turning on / off the magnetic force is provided on the bottom of the gutter,
The undissolved metal is adhered to the trough bottom by tilting the tilted trough to which magnetic force is applied to the downstream side of the tilted trough,
A method for separating and collecting undissolved metal, characterized in that the deposit is dropped into the melting tank by tilting the inclined trough toward the melting tank to cut off the magnetic force.
【請求項2】 上記傾注樋をその下流側に傾けてめっき
浴の方向へ通過させためっき液を、さらに中空フィルタ
を通過させることを特徴とする請求項1記載の未溶解金
属の分離回収方法。
2. The method for separating and recovering undissolved metal according to claim 1, wherein the tilting trough is tilted to the downstream side and passed through in the direction of the plating bath, and further passed through a hollow filter. .
【請求項3】 上記傾注樋の傾き方向の変更をその上を
通過させためっき液の累積流量に基づき自動的に行うこ
とを特徴とする請求項1又は2記載の未溶解金属の分離
回収方法。
3. The method for separating and recovering undissolved metal according to claim 1, wherein the tilt direction of the tilting gutter is automatically changed based on the cumulative flow rate of the plating solution passed therethrough. .
JP7004804A 1995-01-17 1995-01-17 Method for separating and recovering undissolved metal Withdrawn JPH08193300A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7004804A JPH08193300A (en) 1995-01-17 1995-01-17 Method for separating and recovering undissolved metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7004804A JPH08193300A (en) 1995-01-17 1995-01-17 Method for separating and recovering undissolved metal

Publications (1)

Publication Number Publication Date
JPH08193300A true JPH08193300A (en) 1996-07-30

Family

ID=11593958

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7004804A Withdrawn JPH08193300A (en) 1995-01-17 1995-01-17 Method for separating and recovering undissolved metal

Country Status (1)

Country Link
JP (1) JPH08193300A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020038224A (en) * 2000-11-17 2002-05-23 이구택 apparatus for preventing an oxidation on non-coating surface of strip and removing a metal precipitation material
JP2007146286A (en) * 2005-10-25 2007-06-14 Ebara Corp Electroless plating apparatus and electroless plating method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020038224A (en) * 2000-11-17 2002-05-23 이구택 apparatus for preventing an oxidation on non-coating surface of strip and removing a metal precipitation material
JP2007146286A (en) * 2005-10-25 2007-06-14 Ebara Corp Electroless plating apparatus and electroless plating method

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