JPH07233500A - Method for removing metallic ion impurity - Google Patents

Method for removing metallic ion impurity

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Publication number
JPH07233500A
JPH07233500A JP4646894A JP4646894A JPH07233500A JP H07233500 A JPH07233500 A JP H07233500A JP 4646894 A JP4646894 A JP 4646894A JP 4646894 A JP4646894 A JP 4646894A JP H07233500 A JPH07233500 A JP H07233500A
Authority
JP
Japan
Prior art keywords
chamber
processing
electrolytic
plating
metal ion
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
JP4646894A
Other languages
Japanese (ja)
Inventor
Kenji Terada
憲司 寺田
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.)
KYB Corp
Original Assignee
Kayaba Industry Co 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 Kayaba Industry Co Ltd filed Critical Kayaba Industry Co Ltd
Priority to JP4646894A priority Critical patent/JPH07233500A/en
Publication of JPH07233500A publication Critical patent/JPH07233500A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To simplify an equipment and to effectively utilize the electric power by making use of the advantage of a means for removing metallic impurities by electrolytic separation. CONSTITUTION:The inside of an electrolytic working tank A used in the pretreatment for plating is separated with a metal ion-permeable ion-exchange membrane 4 into a working chamber 5 filled with a working soln. and a precipitation chamber 6 filled with a processing soln. 7 on the electrode 8 side. The metallic ion impurities 10 contained in the working soln. 2 are permeated through the membrane 4 into the precipitation chamber 6 simultaneously with the electrolytic working in the chamber 5, allowed to react with the processing soln. 7 in the chamber 6 and precipitated. The soln. 7 contg. the precipitate is recirculated to the precipitation chamber 6 through a separator 11 from the chamber 6, and the precipitate is separated from the soln. 7 with the separator 11 and discharged.

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、めっき加工にとって
有害な金属イオン不純物のめっき原液への混入を防止す
るための金属イオン不純物の除去方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for removing metal ion impurities for preventing metal ion impurities harmful for plating processing from being mixed into a plating stock solution.

【0002】[0002]

【従来の技術】めっき加工に当って、めっき槽内のめっ
き原液は勿論のこと、前処理として被めっき物(以下、
加工物という)を酸洗したりエッチングする電解加工槽
内の電解酸洗液やエッチング液(以下、めっき原液を含
めて加工液という)に含まれる塵埃や油脂或いは金属イ
オン等の不純物は、めっき層の品質低下や加工速度の低
下をもたらして有害であることから極力除去してやるこ
とが望ましい。
2. Description of the Related Art In plating, not only the undiluted solution in the plating tank but also the object to be plated (hereinafter
Impurities such as dust, oil and fat, metal ions, etc., contained in the electrolytic pickling solution and etching solution (hereinafter referred to as processing solution including plating stock solution) in the electrolytic processing tank for pickling and etching It is desirable to remove it as much as possible because it is harmful because it causes deterioration of layer quality and processing speed.

【0003】これら加工液中に含まれる不純物のうち、
塵埃や油脂等は、例えばフィルターなどによって比較的
容易に除去し得るが、金属イオンは、加工液中に溶解し
たかたちで含まれているためにフィルターなどによって
は容易に除去することができない。
Of the impurities contained in these working fluids,
Dust, oil and fat can be relatively easily removed by, for example, a filter, but metal ions cannot be easily removed by a filter because they are contained in the working liquid in a dissolved form.

【0004】したがって、繰り返し行われるめっき加工
に伴って、これら加工液中には金属イオン不純物が次第
に蓄積してくる。
Therefore, metal ion impurities gradually accumulate in these working liquids as the plating process is repeated.

【0005】そのために、加工液中の金属イオン不純物
が一定の濃度に達した時点でこれを廃却処分するか、若
しくは別プロセスで中和処理して再生せざるを得ず、そ
の結果、公害発生や処理コストの高騰などの問題が生じ
る。
For this reason, when the metal ion impurities in the working liquid reach a certain concentration, they have to be discarded or regenerated by neutralization in another process, resulting in pollution. Problems such as generation and soaring processing costs occur.

【0006】そこで、従来、これらの問題点を解決する
ために、電解分離手段による金属イオン不純物の除去方
法、即ち、電解分離法が案出された。
Therefore, in order to solve these problems, a method of removing metal ion impurities by electrolytic separation means, that is, an electrolytic separation method has hitherto been devised.

【0007】この電解分離法は、加工液中に含まれる金
属イオン不純物を連続的に除去する方法で、めっき設備
に付随して電解分離槽からなる処理設備を付設し、この
電解分離槽の内部を金属イオン透過用のイオン交換膜で
処理室と沈殿室とに区画し、かつ、これら処理室と沈殿
室の内部に対して、一方には陽極の電極を他方には陰極
の電極を互いに向かい合わせて配設する。
This electrolytic separation method is a method for continuously removing metal ion impurities contained in the working liquid. A processing facility consisting of an electrolytic separation tank is attached to the plating facility, and the inside of this electrolytic separation tank is attached. Is divided into a treatment chamber and a precipitation chamber by an ion-exchange membrane for permeation of metal ions, and an anode electrode on one side and a cathode electrode on the other side face each other with respect to the insides of these treatment and precipitation chambers. Arrange them together.

【0008】そして、沈殿室内に処理液を満たした状態
でめっき設備におけるめっき槽や電解加工槽内の加工液
を処理室との間で循環させつつ、両電極間に直流電流を
通電してやる。
Then, while the processing liquid is filled in the precipitation chamber, the processing liquid in the plating tank or the electrolytic processing tank in the plating facility is circulated between the processing chamber and the processing liquid, and a direct current is applied between both electrodes.

【0009】これにより、加工液中に含まれる金属イオ
ン不純物がイオン交換膜を通して沈殿室内の処理液中に
透過し、当該処理液と反応して金属水酸化物または金属
酸化物となり、沈殿室の底に沈殿する。
As a result, the metal ion impurities contained in the processing liquid permeate into the processing liquid in the precipitation chamber through the ion exchange membrane, and react with the processing liquid to form metal hydroxide or metal oxide, and the metal ions in the precipitation chamber are discharged. Settle to the bottom.

【0010】このようにして、有害な金属イオン不純物
を沈殿させつつ設備外へと取り出して除去すようにして
いる。
In this way, harmful metal ion impurities are precipitated and taken out of the equipment to be removed.

【0011】[0011]

【発明が解決しようとする課題】そのために、この従来
の電解分離法にあっては、めっき設備の外に金属イオン
不純物を除去するための処理設備である電解分離槽を必
要とし、その結果、設備費が嵩むという不都合をもつ。
Therefore, this conventional electrolytic separation method requires an electrolytic separation tank, which is a treatment equipment for removing metal ion impurities, in addition to the plating equipment. It has the disadvantage of increasing equipment costs.

【0012】また、そればかりでなく、電解分離槽で消
費される電流は、金属イオン不純物の除去のみに使用さ
れるだけで、めっき加工は勿論のこと前処理として行わ
れる加工物の酸洗やエッチング等にも全く寄与せず、そ
の分、消費電力量が新たに必要になってランニングコス
トが高くつくという問題点をも有する。
Not only that, but the current consumed in the electrolytic separation tank is used only for removing metal ion impurities, and not only the plating process but also the pickling of the processed product performed as a pretreatment. There is also a problem that it does not contribute to etching or the like at all, and that power consumption is newly required and the running cost becomes high accordingly.

【0013】したがって、この発明の目的は、電解分離
法による金属イオン不純物の除去手段がもつ利点を活か
しながら、しかも、設備の簡素化と消費電力の有効利用
とを図ることのできる金属イオン不純物の除去方法を提
供することである。
Therefore, an object of the present invention is to utilize the advantages of the means for removing metal ion impurities by the electrolytic separation method, while at the same time simplifying the equipment and effectively utilizing the power consumption. It is to provide a removal method.

【0014】[0014]

【問題を解決するための手段】この発明において、上記
の目的は、めっき加工の前処理工程として使用される電
解加工槽内に直接金属イオン透過用のイオン交換膜を張
設し、当該イオン交換膜により電解加工槽の内部を加工
液で満たした加工室と処理液を満たした電極側の沈殿室
とに区画する。
In the present invention, the above object is to provide an ion exchange membrane for direct metal ion permeation in an electrolytic processing tank used as a pretreatment step of plating, and to perform the ion exchange. The membrane divides the inside of the electrolytic processing tank into a processing chamber filled with the processing liquid and a precipitation chamber on the electrode side filled with the processing liquid.

【0015】そして、加工室内での電解加工行程と同時
に、加工液中に含まれる金属イオン不純物をイオン交換
膜を通して沈殿室側に透過させ、当該沈殿室内の処理液
と反応させて沈殿させる。
Simultaneously with the electrolytic processing step in the processing chamber, the metal ion impurities contained in the processing liquid are permeated to the precipitation chamber side through the ion exchange membrane and reacted with the processing liquid in the precipitation chamber to cause precipitation.

【0016】しかるのち、この沈殿物を含む処理液を沈
殿室から分離器を通して再び沈殿室へと循環させつつ、
当該分離器により処理液の中から沈殿物を分離して取り
出すことにより達成される。
Thereafter, while circulating the treatment liquid containing the precipitate from the precipitation chamber through the separator to the precipitation chamber again,
This is achieved by separating and removing the precipitate from the treatment liquid by the separator.

【0017】[0017]

【作用】すなわち、上記の手段をとることにより、めっ
き加工に当って、前処理工程として行われる電解加工槽
内での加工物の酸洗やエッチング処理時に、加工液中に
遊離した金属イオン不純物はイオン交換膜を通して加工
室内から沈殿室内へと透過し、当該沈殿室内の処理液と
反応して沈殿する。
[Effects] That is, by taking the above means, metal ion impurities liberated in the working fluid during pickling or etching of the workpiece in the electrolytic processing tank, which is performed as a pretreatment step in plating. Permeates from the processing chamber to the precipitation chamber through the ion exchange membrane, and reacts with the processing liquid in the precipitation chamber to precipitate.

【0018】そして、この沈殿物を含む処理液を、沈殿
室から分離器を通して再び沈殿室へと循環してやること
により、金属イオン不純物としての当該沈殿物は分離器
により処理液中から分離されて外部に取り出される。
The treatment liquid containing this precipitate is circulated again from the precipitation chamber through the separator to the precipitation chamber, whereby the precipitate as metal ion impurities is separated from the treatment liquid by the separator and externally Taken out.

【0019】したがって、めっき加工の前処理工程であ
る酸洗やエッチング処理時の電力を利用して同時に金属
イオン不純物の除去が行われることになる。
Therefore, the metal ion impurities are removed at the same time by utilizing the electric power at the time of pickling or etching which is a pretreatment step of the plating process.

【0020】[0020]

【実施例】以下、この発明による金属イオン除去方法
を、実際に適用する装置例を用いて説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The metal ion removing method according to the present invention will be described below with reference to an example of an actually applied apparatus.

【0021】図1に示すように、めっき加工の一般的な
工程システムは、予め加工物に酸洗やエッチング等の前
処理を施すために、先ず、加工物1を前処理槽である電
解酸洗液やエッチング液等の加工液2で満たした電解加
工槽Aに入れる。
As shown in FIG. 1, in a general process system for plating, in order to pretreat a workpiece in advance by pickling, etching, etc., first, the workpiece 1 is treated with an electrolytic acid as a pretreatment tank. It is placed in an electrolytic processing tank A filled with a processing liquid 2 such as a washing liquid or an etching liquid.

【0022】そして、この電解加工槽A内の加工液2で
加工物1に酸洗やエッチング等の前処理を施してからめ
っき槽Bに移し、めっき原液3を満たしためっき槽B内
で加工物1の表面にめっき層を施す。
Then, the workpiece 1 is subjected to pretreatment such as pickling and etching with the processing liquid 2 in the electrolytic processing tank A, and then transferred to the plating tank B, and processed in the plating tank B filled with the plating stock solution 3. A plating layer is applied to the surface of the article 1.

【0023】しかるのちに、このめっき層を施した加工
物1を一次水洗槽Cおよび二次水洗槽Dへと順次に通し
て二度に亙り水洗し、めっき加工を完了する。
Thereafter, the processed product 1 provided with this plating layer is successively passed through the primary water washing tank C and the secondary water washing tank D and rinsed with water twice to complete the plating process.

【0024】上記のめっき加工行程において、特に、め
っき槽B内のめっき原液3の中に金属イオン不純物が存
在すると、先に述べたように、当該金属イオン不純物が
めっき加工に災いをもたらしてめっき層の品質低下や加
工速度の低下をきたす。
In the above plating process, particularly, when metal ion impurities are present in the plating stock solution 3 in the plating tank B, the metal ion impurities cause damage to the plating process as described above, and plating is performed. It causes deterioration of layer quality and processing speed.

【0025】そこで、この金属イオン不純物について考
察してみたところ、当該金属イオン不純物は、主として
加工物1の前処理工程である電解加工槽Aでの酸洗やエ
ッチング処理時に当該加工物1へと付着する。
Then, when considering the metal ion impurities, the metal ion impurities are mainly transferred to the workpiece 1 during pickling or etching in the electrolytic processing tank A which is a pretreatment step of the workpiece 1. Adhere to.

【0026】そして、めっき加工行程の進行に伴って、
当該金属イオン不純物が、電解加工槽Aから加工物1と
共にめっき槽Bに持ち込まれ、めっき原液3の中へと蓄
積されていく。
Then, as the plating process progresses,
The metal ion impurities are brought into the plating tank B from the electrolytic processing tank A together with the workpiece 1 and are accumulated in the plating stock solution 3.

【0027】このことから、電解加工槽A内の加工液2
の中に含まれる金属イオン不純物を除去してやれば、当
該金属イオン不純物のめっき槽B内への持ち込みを減ら
してめっき原液3の中の金属イオン不純物を低減させ得
ることが分かった。
From this, the machining liquid 2 in the electrolytic machining tank A is
It has been found that if the metal ion impurities contained in the solution are removed, the carry-in of the metal ion impurities into the plating bath B can be reduced and the metal ion impurities in the plating stock solution 3 can be reduced.

【0028】一方、めっき加工の前処理工程である電解
加工槽Aでは、もともと電力を用いて加工物1の電解酸
洗やエッチング処理が行われている。
On the other hand, in the electrolytic processing tank A, which is a pretreatment process for plating, the electric power is originally used to perform electrolytic pickling and etching of the workpiece 1.

【0029】そこで、これらの現状に基づいて、当該実
施例にあっては、以下に述べるような金属イオン不純物
の除去手段を採用した。
Therefore, based on these circumstances, in the present embodiment, the following means for removing metal ion impurities was adopted.

【0030】すなわち、図2にみられるように、例えば
クロムめっき加工の前処理工程として用いられている電
解加工槽A内に直接金属イオン透過用のイオン交換膜4
を張設し、このイオン交換膜4によって電解加工槽Aの
内部を加工室5と電極8側の沈殿室6とに区画する。
That is, as shown in FIG. 2, for example, the ion exchange membrane 4 for directly permeating metal ions is placed in the electrolytic processing tank A used as a pretreatment step for chromium plating.
And the inside of the electrolytic processing tank A is partitioned by the ion exchange membrane 4 into a processing chamber 5 and a precipitation chamber 6 on the electrode 8 side.

【0031】上記加工室5の内部には、前処理用の電解
酸洗液またはエッチング液等の加工液2をそのまま入
れ、また、沈殿室6の内部は、炭酸ソーダ水溶液等の処
理液7で満たしてやる。
Inside the processing chamber 5, the processing liquid 2 such as an electrolytic pickling solution or an etching solution for pretreatment is put as it is, and inside the precipitation chamber 6 is a processing liquid 7 such as an aqueous solution of sodium carbonate. I'll meet you.

【0032】そして、加工物1を加工室5内の加工液2
中に浸し、この加工物1を陽極の電極として、また、沈
殿室6内の電極8を陰極としてこれらの間に整流器9を
通して直流電流を通電してやる。
Then, the workpiece 1 is processed into the processing liquid 2 in the processing chamber 5.
The processed material 1 is used as an anode electrode and the electrode 8 in the precipitation chamber 6 is used as a cathode, and a DC current is passed through a rectifier 9 between them.

【0033】これにより、加工物1に前処理工程である
電解加工が施されると同時に、加工液2中に含まれる金
属不純物10が陽イオンとなってイオン交換膜4を通り
沈殿室6内の処理液7中に透過してくる。
As a result, the workpiece 1 is subjected to electrolytic processing, which is a pretreatment step, and at the same time, the metal impurities 10 contained in the processing liquid 2 become cations and pass through the ion exchange membrane 4 to settle in the precipitation chamber 6. Permeate into the treatment liquid 7.

【0034】このイオン交換膜4を透過してきた金属イ
オン不純物10は、沈殿室6内の処理液7と反応して金
属水酸化物となり、当該沈殿室6の底に沈殿する。
The metal ion impurities 10 that have permeated the ion exchange membrane 4 react with the treatment liquid 7 in the precipitation chamber 6 to form metal hydroxides, which precipitate on the bottom of the precipitation chamber 6.

【0035】そこで、この沈殿物を含む処理液7を沈殿
室6から分離器11を通して再び沈殿室6へと循環させ
つつ、当該分離器11により処理液7中から沈殿物を分
離して取り出す。
Therefore, while the treatment liquid 7 containing the precipitate is circulated from the precipitation chamber 6 through the separator 11 to the precipitation chamber 6 again, the separator 11 separates the precipitate from the treatment liquid 7 and takes it out.

【0036】そして、この取り出された金属水酸化物
は、スラッジとして処理するなり或いは有効利用できる
ものは原材料として売却する。
The metal hydroxide taken out is treated as sludge, or if it can be effectively used, it is sold as a raw material.

【0037】かくして、めっき加工にとって有害な金属
イオン不純物は、めっき加工の前処理工程である酸洗や
エッチング処理時の電力を利用して同時にその除去が行
われることになる。
Thus, the metal ion impurities harmful to the plating process are removed at the same time by utilizing the electric power at the time of pickling or etching which is a pretreatment process of the plating process.

【0038】ただし、上記の手段にあっても、イオン交
換膜4を通して沈殿室6に透過してきた金属イオン不純
物はその殆どが金属水酸化物となって沈殿するが、その
一部はそのままの形で処理液7中に残存し、当該処理液
7中の金属イオン不純物の濃度が次第に増加してくる。
However, even with the above means, most of the metal ion impurities that have permeated into the precipitation chamber 6 through the ion exchange membrane 4 are precipitated as metal hydroxides, but some of them remain as they are. Thus, the concentration of the metal ion impurities remaining in the treatment liquid 7 gradually increases.

【0039】したがって、一定の濃度になった段階で処
理液7を更新する必要があるが、しかし、この濃度の増
加速度は極めて低く、したがって、長期間に亙っての使
用が可能である。
Therefore, it is necessary to renew the processing liquid 7 at a stage where the concentration becomes constant, but the increasing rate of this concentration is extremely low, and therefore it can be used for a long period of time.

【0040】そうかと言っても、いずれは処理液7の更
新が必要となるので、その場合には中和イオン交換処理
等で処理液7を無害化して放流する。
Even so, the treatment liquid 7 will eventually need to be renewed. In that case, the treatment liquid 7 is detoxified and discharged by neutralization ion exchange treatment or the like.

【0041】なお、これまでの実施例にあっては、加工
物1を陽極として前処理を行うクロムめっき等の場合を
例にとって説明してきた。
In the above-mentioned embodiments, the case of chromium plating or the like in which the workpiece 1 is used as an anode for pretreatment has been described as an example.

【0042】しかし、亜鉛めっき等にあっては、加工物
1を陽極としてもまた陰極としても前処理を行うことが
できる。
However, in the case of galvanizing or the like, the pretreatment can be carried out using the work piece 1 as an anode or a cathode.

【0043】したがって、この場合にあっても加工物1
を陽極とし、かつ、沈殿室6内の処理液7に硫酸ソーダ
水溶液等を用いてやることにより、同様にして、金属イ
オン不純物を金属酸化物として沈殿させつつ除去するこ
とができる。
Therefore, even in this case, the workpiece 1
Is used as the anode and a sodium sulfate aqueous solution or the like is used as the treatment liquid 7 in the precipitation chamber 6, in the same manner, the metal ion impurities can be removed while being precipitated as metal oxides.

【0044】[0044]

【発明の効果】以上のように、この発明によれば、めっ
き加工の前処理工程として使用されている電解加工槽を
用い、かつ、前処理加工時の電力を利用して同時に金属
イオン不純物の除去をも行うことがで、したがって、め
っき設備の簡素化と共に消費電力の有効利用をも図るこ
とができる利点を有する。
As described above, according to the present invention, the electrolytic processing tank used as the pretreatment step of plating is used, and the electric power at the time of the pretreatment is utilized to simultaneously remove the metal ion impurities. Since it can be removed, there is an advantage that the plating facility can be simplified and the power consumption can be effectively utilized.

【0045】また、上記と合わせて、前処理用加工液の
劣化をも抑制してその寿命を延ばすことが可能になるの
である。
Further, in addition to the above, it is possible to suppress the deterioration of the pretreatment processing liquid and extend the life thereof.

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

【図1】めっき加工設備の一般的な工程例を示すシステ
ム図である。
FIG. 1 is a system diagram showing an example of a general process of a plating facility.

【図2】上記図1のシステム図において、この発明を実
施するための電解加工槽の構造例を示す概略図である。
FIG. 2 is a schematic diagram showing a structural example of an electrolytic processing tank for carrying out the present invention in the system diagram of FIG.

【符号の説明】[Explanation of symbols]

A 電解加工槽 2 加工液 4 イオン交換膜 5 加工室 6 沈殿室 7 処理液 8 電極 10 金属イオン不純物 11 分離器 A Electrolytic processing tank 2 Processing liquid 4 Ion exchange membrane 5 Processing chamber 6 Precipitation chamber 7 Processing liquid 8 Electrode 10 Metal ion impurity 11 Separator

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 めっき加工の前処理工程として使用する
電解加工槽内に直接金属イオン透過用のイオン交換膜を
張設して、当該イオン交換膜により電解加工槽の内部を
加工液で満たした加工室と処理液を満たした電極側の沈
殿室とに区画し、この加工室内での電解加工行程と同時
に、加工液中に含まれる金属イオン不純物をイオン交換
膜を通して沈殿室側に透過させ、当該金属イオン不純物
を沈殿室内の処理液と反応させて沈殿させたのち、この
処理液を沈殿室から分離器を通して再び沈殿室へと循環
させつつ、当該分離器により処理液中から沈殿物を分離
して取り出すことを特徴とする金属イオン不純物の除去
方法。
1. An ion exchange membrane for directly permeating metal ions is stretched in an electrolytic processing tank used as a pretreatment step for plating, and the inside of the electrolytic processing tank is filled with the processing liquid by the ion exchange membrane. It is divided into a processing chamber and a precipitation chamber on the electrode side filled with the processing liquid, and at the same time as the electrolytic processing step in this processing chamber, metal ion impurities contained in the processing liquid are permeated to the precipitation chamber side through an ion exchange membrane, After the metal ion impurities are reacted with the treatment liquid in the precipitation chamber to cause precipitation, the treatment liquid is circulated from the precipitation chamber through the separator to the precipitation chamber again, while the separator separates the precipitate from the treatment liquid. A method for removing metal ion impurities, characterized in that
JP4646894A 1994-02-21 1994-02-21 Method for removing metallic ion impurity Pending JPH07233500A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4646894A JPH07233500A (en) 1994-02-21 1994-02-21 Method for removing metallic ion impurity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4646894A JPH07233500A (en) 1994-02-21 1994-02-21 Method for removing metallic ion impurity

Publications (1)

Publication Number Publication Date
JPH07233500A true JPH07233500A (en) 1995-09-05

Family

ID=12748011

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4646894A Pending JPH07233500A (en) 1994-02-21 1994-02-21 Method for removing metallic ion impurity

Country Status (1)

Country Link
JP (1) JPH07233500A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009215581A (en) * 2008-03-07 2009-09-24 Okuno Chem Ind Co Ltd Method of removing metallic impurities in trivalent chromium bath

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009215581A (en) * 2008-03-07 2009-09-24 Okuno Chem Ind Co Ltd Method of removing metallic impurities in trivalent chromium bath

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