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JPS6354800B2 - - Google Patents
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JPS6354800B2 - - Google Patents

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Publication number
JPS6354800B2
JPS6354800B2 JP54102183A JP10218379A JPS6354800B2 JP S6354800 B2 JPS6354800 B2 JP S6354800B2 JP 54102183 A JP54102183 A JP 54102183A JP 10218379 A JP10218379 A JP 10218379A JP S6354800 B2 JPS6354800 B2 JP S6354800B2
Authority
JP
Japan
Prior art keywords
gold plating
plating solution
gold
harmful metals
metal scavenger
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.)
Expired
Application number
JP54102183A
Other languages
Japanese (ja)
Other versions
JPS5629697A (en
Inventor
Kazuhiro Higuchi
Mitsuru Shibata
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.)
NIPPON EREKUTOROPUREITEINGU ENJINYAAZU KK
Original Assignee
NIPPON EREKUTOROPUREITEINGU ENJINYAAZU KK
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 NIPPON EREKUTOROPUREITEINGU ENJINYAAZU KK filed Critical NIPPON EREKUTOROPUREITEINGU ENJINYAAZU KK
Priority to JP10218379A priority Critical patent/JPS5629697A/en
Publication of JPS5629697A publication Critical patent/JPS5629697A/en
Publication of JPS6354800B2 publication Critical patent/JPS6354800B2/ja
Granted legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は金めつき液の回復方法に関するもので
ある。 一般に金めつき液は使用中に前処理液の持込
み、めつき物素材や治具、ラツク、リード線等の
溶解に因り有害金属が混入し易く汚染され易いも
のであり、しかも一度汚染されてしまうとその有
害金属が金析出物に悪影響を与え易くなり、その
ようになれば金めつき液はもはや使用不可能にな
つて新しい液と交換せざるを得ないものである。
そして汚染された金めつき液は金属金の回収処理
にまわされるが、金属金のロスは多く回収費用も
相当掛かりしかも金属金以外の金めつき液中の使
用薬品が全く無駄となつてしまうためその損失は
多大なものがある。一方で、金めつき液以外の技
術分野、例えば廃水処理、では有害金属を除去す
るための薬品が既に開発され使用されているけれ
ども、金めつき液は周知のように完成されたもの
でそれ自体が非常に精緻にして微妙な内容の薬品
になつているため、他の薬品を金めつき液中へ入
れることは金めつき液にマイナスの要素を与え特
性を劣化させてしまうのではないかとの懸念もあ
つて、金めつき液中に金めつきの用途以外の薬品
を入れることが全く不可能視されているのが実情
であつた。 然しながら、完成された内容の金めつき液にマ
イナスの影響を与えずに有害金属を除去できれ
ば、汚染された金めつき液でも回復して再使用で
きるとの課題の下で本発明者は種々の研究を重ね
た結果、金属捕捉剤それもキレート作用で有害金
属を捕捉できるものを用いれば所望の意図が達成
できるとの知見を得て本発明を開発するに至つた
ものである。そして、具体的には、本発明は金を
シアン化金カリウムの形で含有し遊離シアンを含
まない金めつき液に、汚染として混入した有害な
金属だけを、金属捕捉剤としての有機キレート化
剤又はそのイオウ化合物にて沈澱せしめ分離して
その有害金属を除去するようにしたことを特徴と
する金めつき液の回復方法を提供せんとするもの
である。 以下、この詳細を説明する。先ず本発明で対象
とする金めつき液は、金をシアン化金カリウムの
形で含有し遊離シアンを含まない金めつき液であ
る。遊離シアンを多量に含有したシアン系金めつ
き液に於ては混入した金属不純物はただちにシア
ンと錯体を形成してしまうため、これを沈澱分離
するには多量の金属捕捉剤を必要とし、従つて金
属金のロスも多量となる。また今日の金めつき技
術に於ては遊離シアンを多量に含有する金めつき
液の使用はもはや限られたものであり、従つて本
発明は遊離シアンを含有する金めつき液を対象と
するものではない。 金めつき液に汚染として混入する有害な金属と
は前処理液の混入とか、めつき物素材、治具、ラ
ツク、リード線等の溶解とかに因つて混入してく
る金属で、「純金めつき液」では銅、鉛、錫、ニ
ツケルを主として指称し、通常使用中に於て混入
する濃度は銅5〜100ppm、鉛2〜20ppm、錫10
〜50ppm、ニツケル50〜500ppmの範囲であり、
銅の混入で金めつき液が汚染すると析出物が本来
の無光沢黄金色を呈さず赤褐色となり、又他の金
属即ち鉛、錫、ニツケルの混入に因る汚染があれ
ば共析により析出物が光沢となつて純度の低下を
来たし、純金めつき本来の特徴である耐熱性その
他に悪影響を与えることとなる。そして「合金金
めつき液」では銅、鉛が主として有害な金属とし
て混入し易く、銅10〜50ppm、鉛3〜20ppmが汚
染範囲で、いずれの場合も金析出物は赤褐色とな
つて好ましくないものである。 金属捕捉剤とは、有機キレート化剤又はそのイ
オウ化合物を意味し、キレート作用にて水溶液中
に於て重金属イオンと会合するとただちに極めて
溶解度が低い不溶性化合物を形成し凝集沈澱を生
じさせるものである。例えば、ジメチルグリオキ
シムのようにニツケルと化合すると不溶性の沈澱
物を生じるものである。特に、イオウ化合物は金
属イオンと結合し不溶性の沈澱物を作り易い。ま
た、有機キレート化剤の例としては、8―キノリ
ノール[C9H7NO]を挙げることができ、そのイ
オウ化物としては、メルカプトベンゾチアゾール
[C7H5NS2]を挙げることができる。そして、水
溶液の形で「カプロン」「カパトール」等の商品
名で通常市販されているものを使用することがで
きる。 このような金属捕捉剤と併用する活性炭は市販
の粉末状のものを使用するものとし、金めつき液
中へ適量添加の後撹拌してろ過することによつて
有害なる重金属の除去のみでなく金めつき液中の
有機汚染物や未反応の捕捉剤をも取り除くことが
できる。 次に実施例を述べる。 実施例 1 金めつき液:中性純金めつき液 1 (組 成) クエン酸カリウム 100g/ リン酸1カリウム 50g/ シアン化金カリウム 10g/ PH 6.5に調整 汚染源 :硫酸ニツケル 1400mg 硫酸第二鉄アンモニウム 700mg 硫酸銅 70mg 電解条件:電流密度 0.5A/dm2 温 度 65℃ 時 間 5分間 上記の条件で、金めつき液中に汚染源を故意に
添加し、この金めつき液を電解したところ析出物
は赤褐色の好ましくない外観を呈した。 この汚染された金めつき液に金属捕捉剤を10
ml/添加し、50℃で10分間撹拌した後ろ別し
た。そして汚染源としての有害金属を除去した金
めつき液に金属金2g/を補給し同様な条件で
電解したところ汚染前の析出物と同等な半光沢で
均一な黄金色を呈する良好な析出物が得られた。 金属金を補給する直前の金めつき液を原子吸光
法により分析したところ次の結果を得た。
The present invention relates to a method for recovering gold plating solution. In general, gold plating solutions are easily contaminated with harmful metals due to the introduction of pre-treatment solutions and the melting of plating materials, jigs, racks, lead wires, etc. during use, and once contaminated. If this happens, the harmful metals tend to have an adverse effect on the gold deposits, and if this happens, the gold plating solution becomes unusable and must be replaced with a new solution.
The contaminated gold plating solution is then sent to the recovery process for metallic gold, but there is a lot of loss of metallic gold and the recovery costs are considerable, and the chemicals used in the gold plating solution other than metallic gold are completely wasted. Therefore, the losses are enormous. On the other hand, although chemicals for removing harmful metals have already been developed and used in technical fields other than gold plating solutions, such as wastewater treatment, gold plating solutions are well-known and have not yet been perfected. Since the gold-plating liquid itself is a very sophisticated and delicate chemical, adding other chemicals to the gold-plating liquid will give the gold-plating liquid negative elements and deteriorate its properties. Due to this concern, the reality was that it was considered completely impossible to add chemicals for purposes other than gold plating to the gold plating solution. However, if harmful metals can be removed without negatively impacting the finished gold plating solution, the inventors of the present invention have made various efforts based on the idea that even contaminated gold plating solution can be recovered and reused. As a result of repeated research, the present invention was developed based on the knowledge that the desired purpose could be achieved by using a metal trapping agent that can trap harmful metals through chelating action. Specifically, the present invention uses an organic chelate as a metal scavenger to remove only harmful metals mixed as contaminants into a gold plating solution that contains gold in the form of potassium gold cyanide and does not contain free cyanide. It is an object of the present invention to provide a method for recovering a gold plating solution, which is characterized in that harmful metals are removed by precipitation and separation with a gold plating agent or its sulfur compound. The details will be explained below. First, the gold plating solution targeted by the present invention is a gold plating solution that contains gold in the form of potassium gold cyanide and does not contain free cyanide. In a cyanide-based gold plating solution containing a large amount of free cyanide, metal impurities mixed in immediately form a complex with cyanide, so a large amount of metal scavenger is required to precipitate and separate this. As a result, a large amount of metal gold is lost. Furthermore, in today's gold plating technology, the use of gold plating solutions containing large amounts of free cyanide is now limited, and therefore the present invention is directed to gold plating solutions containing free cyanide. It's not something you do. Harmful metals that get mixed into the gold plating solution as contaminants are metals that come into the gold plating solution as a result of mixing with the pretreatment solution or melting of plating materials, jigs, racks, lead wires, etc. "Gluing liquid" mainly refers to copper, lead, tin, and nickel, and the concentrations that are mixed in during normal use are 5 to 100 ppm of copper, 2 to 20 ppm of lead, and 10 ppm of tin.
~50ppm, nickel ranges from 50 to 500ppm,
If the gold plating solution is contaminated by copper, the precipitate will not have the original matte golden color but will turn reddish brown.If there is contamination due to the contamination of other metals, such as lead, tin, or nickel, the precipitate will become eutectoid. This results in luster and a decrease in purity, which adversely affects the heat resistance and other characteristics that are inherent to pure gold plating. In "alloy gold plating solution", copper and lead are the main harmful metals that are easily mixed in, and the contamination range is 10 to 50 ppm copper and 3 to 20 ppm lead, and in both cases, gold deposits turn reddish brown, which is undesirable. It is something. A metal scavenger refers to an organic chelating agent or its sulfur compound, and when it combines with heavy metal ions in an aqueous solution due to its chelating action, it immediately forms an insoluble compound with extremely low solubility and causes coagulation and precipitation. . For example, dimethylglyoxime produces an insoluble precipitate when combined with nickel. In particular, sulfur compounds tend to combine with metal ions and form insoluble precipitates. An example of the organic chelating agent is 8-quinolinol [C 9 H 7 NO], and an example of its sulfide is mercaptobenzothiazole [C 7 H 5 NS 2 ]. It is also possible to use those commonly commercially available in the form of aqueous solutions under trade names such as "Capron" and "Capatol." Activated carbon used in combination with such metal trapping agents should be commercially available in powder form, and by adding an appropriate amount to the gold plating solution, stirring and filtering, it is possible to not only remove harmful heavy metals, but also to remove harmful heavy metals. Organic contaminants and unreacted scavengers in the gold plating solution can also be removed. Next, an example will be described. Example 1 Gold plating solution: Neutral pure gold plating solution 1 (Composition) Potassium citrate 100g/ Monopotassium phosphate 50g/ Potassium gold cyanide 10g/ Adjusted to PH 6.5 Contamination source: Nickel sulfate 1400mg Ferric ammonium sulfate 700mg Copper sulfate 70mg Electrolytic conditions: Current density 0.5A/dm 2 Temperature 65℃ Time 5 minutes Under the above conditions, when a contamination source was intentionally added to the gold plating solution and the gold plating solution was electrolyzed, precipitation occurred. The material had an unpleasant reddish-brown appearance. Add 10% of metal scavenger to this contaminated gold plating solution.
ml/ml was added, stirred at 50°C for 10 minutes, and then separated. Then, when 2g/g of metallic gold was added to the gold plating solution from which harmful metals as a contamination source had been removed and electrolysis was carried out under the same conditions, a good precipitate was obtained that had the same semi-gloss and uniform golden color as the pre-contamination precipitate. Obtained. The gold plating solution immediately before the addition of metallic gold was analyzed by atomic absorption spectroscopy, and the following results were obtained.

【表】 上表より金属捕捉剤を金めつき液中に添加して
も金属金はそれ程減少せず実用範囲内の減少値で
あること、そして、この減少分の金属金を補給し
電解により得た析出物は良好なものであり、析出
物の色調や外観よりして金属捕捉剤が金めつき液
にマイナスの影響を全然与えていないことが確認
できた。そして肝心の有害な金属はニツケル及び
銅が激減し鉄もそれ相応に除去されていることが
判明した。有害金属が金析出物に悪影響を及ぼす
量は前述の如く、純金めつき液ではニツケル50〜
500ppmそして銅5〜100ppmの範囲であり、上表
で示すように残存ニツケルが5.1ppmそして同じ
く銅が0.2ppmであれば、十二分に金めつき液は
回復したことを意味する。 実施例 2 金めつき液:中性純金めつき液(実施例1と同
様) 汚染源 :硫酸ニツケル 800mg 硫酸第二鉄アンモニウム 400mg 硫酸銅 280mg 電解条件:電流密度 0.5A/dm2 温 度 65℃ 時 間 5分間 上記の条件で、金めつき液中に汚染源を故意に
添加しこの金めつき液を電解したところ析出物は
赤褐色の好ましくない外観を呈した。 この汚染された金めつき液に金属捕捉剤を1.5
ml/添加し、60℃で30分間撹拌した後更に活性
炭2g/を加え30分間撹拌してろ別したとこ
ろ、液は澄んだ淡緑色透明のものになつた。そし
て有害金属を除去した金めつき液を同様な条件で
電解したところ汚染前の析出物と同等の半光沢で
均一な黄金色を呈した良好な析出物が得られた。 この金めつき液を原子吸光法により分析したと
ころ次の結果が得られた。
[Table] From the table above, it can be seen that even if a metal scavenger is added to the gold plating solution, the amount of metallic gold does not decrease significantly, and the decrease is within the practical range. The obtained precipitate was of good quality, and it was confirmed from the color tone and appearance of the precipitate that the metal scavenger had no negative effect on the gold plating solution. It was also found that the important harmful metals, nickel and copper, were drastically reduced, and iron was also removed accordingly. As mentioned above, the amount of harmful metals that have a negative effect on gold deposits is nickel 50~ in pure gold plating solution.
500 ppm and copper in the range of 5 to 100 ppm, and as shown in the table above, if the residual nickel is 5.1 ppm and the copper is 0.2 ppm, it means that the gold plating solution has more than fully recovered. Example 2 Gold plating solution: Neutral pure gold plating solution (same as Example 1) Contamination source: Nickel sulfate 800mg Ferric ammonium sulfate 400mg Copper sulfate 280mg Electrolytic conditions: Current density 0.5A/dm 2 Temperature 65℃ When a contamination source was intentionally added to the gold plating solution and the gold plating solution was electrolyzed under the above conditions, the precipitate had an unfavorable reddish-brown appearance. Add 1.5% of metal scavenger to this contaminated gold plating solution.
After stirring at 60°C for 30 minutes, 2 g/ml of activated carbon was added, stirring for 30 minutes, and filtering. The liquid became clear and pale green. When the gold plating solution from which toxic metals had been removed was electrolyzed under the same conditions, a good precipitate was obtained that had the same semi-gloss and uniform golden color as the pre-contaminated precipitate. When this gold plating solution was analyzed by atomic absorption spectroscopy, the following results were obtained.

【表】 上表より金属捕捉剤及び活性炭を金めつき液中
に添加しても金属金の減少は非常に僅で実用範囲
内の減少値であること、そして析出物の色調や外
観より判断して金属捕捉剤の添加は金めつき液に
悪影響を与えないばかりか、活性炭処理を併用す
ることでめつき液の浄化も同時に為されることが
確認できた。そして、更に、汚染源としての有害
金属はニツケル及び鉄はあまり除去されていない
けれども銅は激減しており、銅の十分な除去のみ
でもこの金めつき液は回復したに等しい。尚、実
施例1に比べ、金属捕捉剤は微量の1.5ml/し
か加えていないので、添加量を増せば実施例1と
同じようにニツケル及び鉄も十分除去可能と思わ
れる。 実施例 3 金めつき液:酸性合金金めつき液 1 (組 成) クエン酸カリウム 50g/ クエン酸 50g/ 硫酸コバルト 5g/ シアン化金カリウム 10g/ PH 3.5に調整 汚染源 :酢酸鉛 20mg 硫酸銅 80mg 電解条件:電流密度 1.0A/dm2 温 度 32℃ 時 間 10分間 上記の条件で、金めつき液中に汚染源を故意に
加え電解したところ析出物は赤褐色で且つむらの
ある好ましくない外観を呈した。 この汚染された金めつき液に金属捕捉剤2ml/
添加し、50℃で10分間撹拌した後、更に活性炭
0.5g/を添加、撹拌してただちにろ別した。
金めつき液に必要成分として存在している金属コ
バルトの減少が見込まれるため原子吸光法により
測定しその不足分を補充し同様の条件で電解した
ところ、析出物は汚染前と全く変らない鏡面光沢
の黄金色を呈した。分析値は次の通りである。
[Table] From the table above, it can be seen that even if a metal scavenger and activated carbon are added to the gold plating solution, the reduction in metallic gold is very small and is within the practical range, and it can be judged from the color tone and appearance of the precipitates. It was confirmed that not only does the addition of a metal scavenger have no adverse effect on the gold plating solution, but also that the plating solution can be purified at the same time by using activated carbon treatment. Furthermore, although nickel and iron have not been significantly removed as harmful metals as contamination sources, copper has been drastically reduced, and sufficient removal of copper is equivalent to recovering the gold plating solution. It should be noted that compared to Example 1, only a small amount of metal scavenger was added, 1.5 ml/ml, so it seems that if the amount added is increased, nickel and iron can be sufficiently removed as in Example 1. Example 3 Gold plating solution: Acidic alloy gold plating solution 1 (Composition) Potassium citrate 50g / Citric acid 50g / Cobalt sulfate 5g / Potassium gold cyanide 10g / Adjusted to PH 3.5 Contaminant sources: Lead acetate 20mg Copper sulfate 80mg Electrolysis conditions: Current density 1.0A/dm 2 Temperature 32℃ Time 10 minutes Under the above conditions, when a contamination source was intentionally added to the gold plating solution and electrolysis was performed, the precipitate was reddish brown and had an undesirable uneven appearance. presented. Add 2 ml of metal scavenger to this contaminated gold plating solution.
After adding activated carbon and stirring for 10 minutes at 50℃,
0.5g/ was added, stirred and immediately filtered.
Metallic cobalt, which is present as a necessary component in gold plating solution, is expected to decrease, so we measured it using atomic absorption spectrometry, replenished the missing amount, and electrolyzed under the same conditions.The deposits were mirror-like, completely unchanged from before contamination. It had a shiny golden color. The analytical values are as follows.

【表】 上表より明らかな如く、金属捕捉剤及び活性炭
を金めつき液中に添加しても金属金の減少はそれ
程大きくなく実用範囲内の減少であること、そし
て析出物の色調や外観からして金属捕捉剤及び活
性炭の添加が金めつき液に悪影響を与えていない
ことが確認できた。そして、有害金属は鉛がそれ
程減少していないけれども銅が減少し合金金めつ
き液で汚染源としての銅が悪影響を与える10〜
50ppmの範囲外になつていることからみてこの金
めつき液は十分回復したものと判断される。 以上説明したように本発明によれば、金めつき
液を汚染し従来新らしい金めつき液との交換を強
いていた有害な金属だけを、金めつき液中へ金属
捕捉剤としてのキレート作用を行なう有機キレー
ト化剤又はそのイオウ化合物、を添加することで
十分に沈澱除去できる。従つて、液中の金属金の
損失は最少限にとどめることができ、加えて金属
捕捉剤を添加しても析出物の色調や外観は汚染前
と変らぬものが得られ金めつき液に全然悪影響を
与えないで済むものであり、そして又金属捕捉剤
と活性炭を併用することにより一層効率よく良好
な状態下で汚染した金めつき液を回復することが
できるものであつて、従来の新液交換に比べれば
その利益は多大なものがある。
[Table] As is clear from the table above, even if a metal scavenger and activated carbon are added to the gold plating solution, the reduction in metallic gold is not so large and is within the practical range, and the color tone and appearance of the precipitates are Therefore, it was confirmed that the addition of the metal scavenger and activated carbon had no adverse effect on the gold plating solution. As for harmful metals, although lead has not decreased that much, copper has decreased, and copper as a source of contamination in alloy gold plating solutions has an adverse effect10~
Judging from the fact that it is outside the 50ppm range, it is judged that this gold plating solution has been sufficiently recovered. As explained above, according to the present invention, only the harmful metals that contaminate the gold plating solution and force the replacement with new gold plating solutions are transferred into the gold plating solution using chelate as a metal scavenger. The precipitate can be sufficiently removed by adding an organic chelating agent or its sulfur compound that acts. Therefore, the loss of metallic gold in the liquid can be kept to a minimum, and even if a metal scavenger is added, the color tone and appearance of the precipitate remain the same as before contamination. It does not cause any adverse effects at all, and by using a metal scavenger and activated carbon together, it is possible to recover contaminated gold plating solution more efficiently and under good conditions, compared to conventional methods. The benefits are significant compared to replacing new fluid.

Claims (1)

【特許請求の範囲】 1 金をシアン化金カリウムの形で含有し遊離シ
アンを含まない金めつき液に、汚染として混入し
た有害な金属だけを、金属捕捉剤としての有機キ
レート化剤又はそのイオウ化合物にて沈澱せしめ
分離してその有害金属を除去するようにしたこと
を特徴とする金めつき液の回復方法。 2 有害な金属を金属捕捉剤で沈澱せしめると共
に活性炭で吸着せしめそして分離する、特許請求
の範囲第1項記載の金めつき液の回復方法。
[Scope of Claims] 1. A gold plating solution containing gold in the form of potassium gold cyanide and containing no free cyanide is freed from harmful metals mixed in as contaminants using an organic chelating agent or its organic chelating agent as a metal scavenger. A method for recovering a gold plating solution, characterized in that harmful metals are removed by precipitation and separation with a sulfur compound. 2. A method for recovering a gold plating solution according to claim 1, wherein harmful metals are precipitated with a metal scavenger, adsorbed with activated carbon, and separated.
JP10218379A 1979-08-13 1979-08-13 Regeneration of gold plating liquid Granted JPS5629697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10218379A JPS5629697A (en) 1979-08-13 1979-08-13 Regeneration of gold plating liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10218379A JPS5629697A (en) 1979-08-13 1979-08-13 Regeneration of gold plating liquid

Publications (2)

Publication Number Publication Date
JPS5629697A JPS5629697A (en) 1981-03-25
JPS6354800B2 true JPS6354800B2 (en) 1988-10-31

Family

ID=14320550

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10218379A Granted JPS5629697A (en) 1979-08-13 1979-08-13 Regeneration of gold plating liquid

Country Status (1)

Country Link
JP (1) JPS5629697A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018070942A (en) * 2016-10-28 2018-05-10 キレスト株式会社 Gold plating solution processing method

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5811799A (en) * 1981-07-16 1983-01-22 Electroplating Eng Of Japan Co Reproducing method of stained gold plating liquid
JPS59182836A (en) * 1983-04-01 1984-10-17 Asahi Glass Co Ltd Fluorine-containing elastomer composition and lining material consisting of it

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5112189B2 (en) * 1972-03-04 1976-04-16
NL7314169A (en) * 1972-11-10 1974-05-14
JPS50656A (en) * 1973-05-08 1975-01-07
JPS51130069A (en) * 1975-05-07 1976-11-12 Hitachi Plant Eng & Constr Co Ltd Method for treating cyanogen-containing waste water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018070942A (en) * 2016-10-28 2018-05-10 キレスト株式会社 Gold plating solution processing method

Also Published As

Publication number Publication date
JPS5629697A (en) 1981-03-25

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