JP3112513B2 - Gold salt solution for gold plating - Google Patents

Gold salt solution for gold plating

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Publication number
JP3112513B2
JP3112513B2 JP03203897A JP20389791A JP3112513B2 JP 3112513 B2 JP3112513 B2 JP 3112513B2 JP 03203897 A JP03203897 A JP 03203897A JP 20389791 A JP20389791 A JP 20389791A JP 3112513 B2 JP3112513 B2 JP 3112513B2
Authority
JP
Japan
Prior art keywords
gold
cyanide
ammonium
plating
solution
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 - Lifetime
Application number
JP03203897A
Other languages
Japanese (ja)
Other versions
JPH0525678A (en
Inventor
衛 平子
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.)
Tanaka Kikinzoku Kogyo KK
Original Assignee
Tanaka Kikinzoku Kogyo 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 Tanaka Kikinzoku Kogyo KK filed Critical Tanaka Kikinzoku Kogyo KK
Priority to JP03203897A priority Critical patent/JP3112513B2/en
Publication of JPH0525678A publication Critical patent/JPH0525678A/en
Application granted granted Critical
Publication of JP3112513B2 publication Critical patent/JP3112513B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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、金メッキ用金塩に用い
るシアン化金アンモニウム溶液に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gold ammonium cyanide solution used for a gold salt for gold plating.

【0002】金メッキに用いる金塩には、従来よりシア
ン化金カリウムがあり、半導体工業をはじめとする多く
の分野で用いられている。こうした金メッキの分野で、
半導体関連工業では、金線ボンディングやTAB技術に
おける接合性の良い柔らかな金を析出させる浴が用いら
れているが、多くの場合は、シアン化金カリウムを用い
る浴が一般的である。シアン化金カリウムを用いる浴で
は、浴のランニングに伴い、浴中にカリウムが蓄積し、
その際にカリウムの共析現象により除々に金メッキ被覆
の硬度が上昇する欠点を有している。しかし、シアン化
金アンモニウムによる浴は、アンモニウムイオンはアン
モニアとして浴より揮散するため蓄積が起こらず、また
アンモニウムは共析現象をおこさないので長期間使用し
てもほぼ一定の硬度の金メッキ被覆が得られる特徴があ
る。この特徴は、前述の半導体関連工業での金線ボンデ
ィングやTAB技術における接合性の良い柔らかな金を
析出させる目的とよく一致し、さらにアルカリ金属イオ
ンを含まないことからマイグレーションの防止等に効果
があると予測され、次世代のメッキ浴として期待されて
いる。本発明の金メッキ用金塩に用いるシアン化金アン
モニウム溶液はこうした要求に対応するためになされた
ものである。
Gold salts used for gold plating include gold potassium cyanide, which has been used in many fields including the semiconductor industry. In the field of gold plating,
In the semiconductor-related industry, baths for depositing soft gold having good bonding properties in gold wire bonding and TAB technology are used, but in many cases, baths using potassium potassium cyanide are generally used. In a bath using potassium potassium cyanide, potassium accumulates in the bath as the bath runs,
At this time, there is a disadvantage that the hardness of the gold plating coating gradually increases due to the eutectoid phenomenon of potassium. However, in a bath using ammonium ammonium cyanide, the accumulation of ammonium ions does not occur because ammonia ions volatilize from the bath as ammonia, and the ammonium plating does not cause an eutectoid phenomenon. There is a feature that is. This feature is in good agreement with the aforementioned purpose of gold wire bonding in the semiconductor-related industry and the purpose of depositing soft gold with good bondability in TAB technology, and furthermore, since it does not contain alkali metal ions, it is effective in preventing migration and the like. It is predicted that there will be, and is expected as a next-generation plating bath. The gold ammonium cyanide solution used for the gold salt for gold plating of the present invention has been made to meet such a demand.

【0003】[0003]

【従来技術とその問題点】シアン化金アンモニウムの製
造に際しては、特公昭48-39158号、あるいは米国特許 3
582269号に例示があり、予めアンモニウム置換したイオ
ン交換樹脂にシアン化金カリウムを通液することにより
得られる。シアン化金アンモニウムは、不安定な金塩で
化1の式に従い、シアン金、アンモニア、シアン化水素
に分解する。
2. Description of the Related Art The production of gold ammonium cyanide is disclosed in Japanese Patent Publication No. 48-39158 or US Pat.
No. 582269, for example, which is obtained by passing potassium potassium cyanide through an ion exchange resin which has been ammonium-substituted in advance. Gold ammonium cyanide is an unstable gold salt that decomposes into gold cyanide, ammonia, and hydrogen cyanide according to the formula (1).

【0004】[0004]

【化1】 Embedded image

【0005】メッキにシアン化金アンモニウムを用いる
場合には、溶液による方法が簡便であるが、保存や経時
変化により分解が進行し、溶液中でシアン化金の黄色の
沈殿が発生する。このシアン化金塩溶液を、金メッキ浴
に使用した場合にはブツやピンホールなどの発生が起こ
りやすくなるため、予め濾過などによりシアン化金を除
いておく必要がある。半導体工業では、回路パターンの
微細化が進んでおり、ブツやピンホールなどの発生は致
命的な欠陥に陥る恐れがある。こうした観点からシアン
化金アンモニウムを使用した浴に用いる金メッキ用金塩
溶液の安定性を増す工夫は、産業上の急務といえる。
In the case of using gold ammonium cyanide for plating, a method using a solution is simple, but decomposition proceeds due to storage or aging, and yellow precipitation of gold cyanide occurs in the solution. When this gold cyanide solution is used in a gold plating bath, bumps and pinholes are likely to occur. Therefore, it is necessary to remove gold cyanide by filtration or the like in advance. In the semiconductor industry, miniaturization of circuit patterns is progressing, and occurrence of bumps, pinholes, and the like may cause fatal defects. From such a point of view, it can be said that a contrivance to increase the stability of the gold salt solution for gold plating used in a bath using gold ammonium cyanide is an urgent need in industry.

【0006】[0006]

【発明の目的】本発明においては、長期間の保存等にお
いても変質のおこりにくいシアン化金アンモニウムを金
塩とする金メッキ用金塩溶液を提供することを目的とす
る。
SUMMARY OF THE INVENTION An object of the present invention is to provide a gold salt solution for gold plating using gold ammonium cyanide, which hardly deteriorates even during long-term storage.

【0007】[0007]

【作用】本発明によるシアン化金アンモニウムを金塩と
する金メッキ用金塩溶液には、シアン化金アンモニウム
の他に、少量のシアン化アンモニウムを含みさらにアン
モニア水で水素イオン濃度を8〜10の間に調整されてい
る。シアン化アンモニウムの添加は、化2、化3に示す
式の化学平衡をずらしシアン化金アンモニウムの安定化
に寄与するためシアン金の生成が防止される。
The gold salt solution for gold plating using gold ammonium cyanide as a gold salt according to the present invention contains a small amount of ammonium cyanide in addition to gold ammonium cyanide and has a hydrogen ion concentration of 8 to 10 with aqueous ammonia. Coordinated in between. The addition of ammonium cyanide shifts the chemical equilibrium of formulas (2) and (3) and contributes to the stabilization of gold ammonium cyanide, thereby preventing the formation of gold cyanide.

【0008】[0008]

【化2】 Embedded image

【0009】さらにアンモニア水はシアン化水素の揮散
を防ぎ、シアン化アンモニウムの安定性向上に寄与す
る。
Further, the ammonia water prevents volatilization of hydrogen cyanide and contributes to the improvement of the stability of ammonium cyanide.

【0010】[0010]

【化3】 Embedded image

【0011】これらの作用により、シアン化金アンモニ
ウムを金塩とする金メッキ用金塩溶液にシアン化アンモ
ニウムとアンモニアが含まれていると、シアン化金アン
モニウムの安定性が増し、長期間の保存等においても変
質のおこりにくいものとなる。またシアン化アンモニウ
ムとアンモニアは、メッキ浴の使用につれて蓄積される
ことなく、除々に揮散するため安定剤として好適であ
る。
By these actions, when ammonium cyanide and ammonia are contained in a gold plating solution containing gold ammonium cyanide as a gold salt, the stability of the gold ammonium cyanide is increased, and long-term storage is possible. Also, it is difficult for deterioration to occur. Ammonium cyanide and ammonia are suitable as stabilizers because they evaporate gradually without accumulating as the plating bath is used.

【0012】シアン化アンモニウムを 0.005〜 1.0%の
濃度範囲とした理由は、 0.005%以下の濃度は安定剤と
しての効果が長続きせずシアン化金を析出し易くなるか
らである。またあまり濃度が高いとメッキ浴に投入した
際に、メッキ浴の液バランスを崩すおそれがあるからで
ある。実際の濃度調整にあたって、シアン化アンモニウ
ム濃度は、シアン化金アンモニウム濃度との割合で1%
前後にしておくのが、操作も容易でメッキ浴の液バラン
スを崩すこともなく好ましい。しかしこれは必ずしもこ
の範囲でなくてもかまわない。
The reason why the concentration of ammonium cyanide is in the range of 0.005 to 1.0% is that if the concentration is 0.005% or less, the effect as a stabilizer does not last long and gold cyanide tends to precipitate. On the other hand, if the concentration is too high, the liquid balance of the plating bath may be lost when it is put into the plating bath. In the actual concentration adjustment, the ammonium cyanide concentration is 1% in proportion to the gold ammonium cyanide concentration.
It is preferable to set them in the front and rear directions, because the operation is easy and the liquid balance of the plating bath is not lost. However, this need not necessarily be in this range.

【0013】アンモニア水で水素イオン濃度を8〜10の
間に調整するのは、水素イオン濃度8以下では、シアン
化水素の揮散が起こりやすく、結果的にシアン化金アン
モニウムの分解がおこるので好ましくない。またシアン
化水素は、有毒であり安全面からも水素イオン濃度8以
下に調整するのは避けた方がよい。水素イオン濃度10以
上では、逆にアンモニアの揮散が激しくなり、臭気が強
く好ましくない。またアンモニアは弱アルカリ性である
ので水素イオン濃度を10以上にするには、大量に添加す
る必要があり、メッキ浴の液バランスを崩し易くなる。
Adjusting the hydrogen ion concentration to between 8 and 10 with aqueous ammonia is not preferred at a hydrogen ion concentration of 8 or less, because hydrogen cyanide tends to volatilize, and as a result, gold ammonium cyanide is decomposed. Further, hydrogen cyanide is toxic, and it is better not to adjust the hydrogen ion concentration to 8 or less from the viewpoint of safety. At a hydrogen ion concentration of 10 or more, on the contrary, the volatilization of ammonia becomes intense and the odor is strong, which is not preferable. In addition, since ammonia is weakly alkaline, it is necessary to add a large amount of hydrogen in order to make the hydrogen ion concentration 10 or more, and the solution balance in the plating bath is easily lost.

【0014】[0014]

【実施例1】本実施例は、シアン化金アンモニウムを含
んだ本発明品の製造方法について示す。5リットルのカ
ラムに詰めた陽イオン交換樹脂3リットルに希硫酸(濃
度5%)20リットルをSV=2で通して、まずイオン交
換樹脂の水素化を行う。ついで、純水を40リットル通し
てよく水洗し、さらに濃度15%のアミド硫酸アンモニウ
ム溶液を通しつつ、液をカラムと槽の間で循環させる。
循環により、溶液の水素イオン濃度は、除々に低下する
のでアンモニア水を添加しつつ水素イオン濃度を4〜7
の範囲で調整することにより、イオン交換樹脂のアンモ
ニウム化を行う。60リットルの純水で再び樹脂を洗浄
し、樹脂塔内に残るアミド硫酸アンモニウム溶液を除
く。本発明品を得るために、次いでシアン化金カリウム
15%、シアン化カリウム0.15%を含む溶液10リットルを
イオン交換樹脂塔に通して、イオン交換樹脂塔内でカリ
ウムとアンモニウムの置換反応をさせる。全量を通液の
後、純水15リットルを通液して樹脂塔内の残液を押しだ
して製品原液とする。製品原液の水素イオン濃度は、5
〜7前後であるのでアンモニア水を加えて水素イオン濃
度を8〜10の範囲に調整する。こうして得られた液は、
シアン化金アンモニウムを約5%、シアン化アンモニウ
ムを約0.03%を含み、長期の保存においてもシアン金を
析出しない。
Example 1 This example shows a method for producing a product of the present invention containing gold ammonium cyanide. First, hydrogenation of the ion exchange resin is performed by passing 20 liters of dilute sulfuric acid (concentration: 5%) at SV = 2 through 3 liters of the cation exchange resin packed in a 5 liter column. Next, 40 liters of pure water are passed through to wash well, and the solution is circulated between the column and the tank while passing a 15% ammonium amide sulfate solution.
Due to the circulation, the hydrogen ion concentration of the solution gradually decreases.
By adjusting the content within the range, ammonium ionization of the ion exchange resin is performed. The resin is washed again with 60 liters of pure water to remove the ammonium amidosulfate solution remaining in the resin tower. Then, to obtain the product of the present invention, potassium gold cyanide
10 liters of a solution containing 15% and 0.15% of potassium cyanide are passed through an ion-exchange resin tower to cause a substitution reaction between potassium and ammonium in the ion-exchange resin tower. After passing the whole amount, 15 liters of pure water is passed through to push out the remaining liquid in the resin tower to obtain a product stock solution. The hydrogen ion concentration of the product stock solution is 5
Since it is about 7 to 7, aqueous ammonia is added to adjust the hydrogen ion concentration to a range of 8 to 10. The liquid thus obtained is
It contains about 5% ammonium cyanide and about 0.03% ammonium cyanide, and does not deposit cyanogen gold even after long-term storage.

【0015】[0015]

【従来例1】実施例と従来例の差は、カリウムとアンモ
ニウムの置換反応をさせる際に通液する液の組成とアン
モニア水を加えて水素イオン濃度を8〜10の範囲に調整
の可否である。実施例1と同様にして操作を行い、カリ
ウムとアンモニウムの置換反応をさせる際に通液する液
の組成を濃度15%のシアン化金カリウム溶液とし、また
アンモニア水を加えて水素イオン濃度を調節しない場合
には、シアン化金アンモニウムを約5%を含む溶液がで
きる。容器に入れ長期の保存を行うとシアン金の黄色の
沈殿が除々に析出できる。
[Prior art 1] The difference between the embodiment and the prior art is that the composition of the liquid to be passed during the substitution reaction of potassium and ammonium and the addition of ammonia water make it possible to adjust the hydrogen ion concentration in the range of 8 to 10. is there. The operation was performed in the same manner as in Example 1 to adjust the composition of the liquid to be passed when the substitution reaction between potassium and ammonium was carried out to a potassium potassium cyanide solution having a concentration of 15%, and to adjust the hydrogen ion concentration by adding aqueous ammonia. Otherwise, a solution containing about 5% gold ammonium cyanide is formed. When stored in a container and stored for a long time, yellow precipitates of cyan gold can be gradually deposited.

【0016】[0016]

【実施例2】シアン化金アンモニウム 5.6%を含み、シ
アン化アンモニウムをそれぞれ0.005、0.03、 0.2、 1.
0%を含みさらに、水素イオン濃度 8.4に調整した溶液
を各々 100ml用意し、共栓式の 300mlの三角フラスコに
入れ、軽く栓をして70℃のウォーターバス中に入れて加
速試験をおこなった。24時間後も各々の容器内の液体に
変化は無かった。
EXAMPLE 2 Ammonium cyanide contained 5.6% of gold ammonium cyanide, and 0.005, 0.03, 0.2 and 1.
100% of each solution containing 0% and adjusted to a hydrogen ion concentration of 8.4 was prepared, placed in a stoppered 300 ml Erlenmeyer flask, lightly stoppered, and placed in a 70 ° C water bath to perform an acceleration test. . After 24 hours, there was no change in the liquid in each container.

【0017】[0017]

【従来例2】シアン化金アンモニウム 5.6%を含む、水
素イオン濃度6.6の溶液 100mlを、共栓式の 300mlの三
角フラスコに入れ、軽く栓をして70℃のウォーターバス
中に入れ、加速試験をおこなった。6時間後には容器内
の液体中に僅かに黄色の沈殿がみられ、24時間後にはさ
らに黄色の沈殿が増加していた。
[Conventional example 2] 100 ml of a solution having a hydrogen ion concentration of 6.6 containing 5.6% of gold ammonium cyanide was placed in a 300 ml conical stoppered Erlenmeyer flask, lightly stoppered and placed in a 70 ° C water bath, followed by an acceleration test. Was done. After 6 hours, a slight yellow precipitate was observed in the liquid in the container, and after 24 hours, the yellow precipitate had further increased.

【0018】[0018]

【比較例1】シアン化金アンモニウム 5.6%を含み、シ
アン化アンモニウムを 0.003%に調整し、水素イオン濃
度 8.4に調整した溶液 100mlを、共栓式の 300mlの三角
フラスコに入れ、軽く栓をして70℃のウォーターバス中
に入れ、加速試験をおこなった。24時間後に容器内の液
体中に僅かに黄色の沈殿がみられた。
[Comparative Example 1] 100 ml of a solution containing 5.6% of gold ammonium cyanide, adjusted to 0.003% of ammonium cyanide, and adjusted to a hydrogen ion concentration of 8.4 was placed in a 300 ml Erlenmeyer flask with a stoppered stopper and lightly stoppered. Into a water bath at 70 ° C. to perform an accelerated test. After 24 hours, a slight yellow precipitate was observed in the liquid in the container.

【0019】[0019]

【比較例2】シアン化金アンモニウム 5.6%を含む、水
素イオン濃度を 8.5に調整した溶液100mlを、共栓式の
300mlの三角フラスコに入れ、軽く栓をして70℃のウォ
ーターバス中に入れ、加速試験をおこなった。24時間後
に容器内の液体中に僅かに黄色の沈殿がみられた。
Comparative Example 2 100 ml of a solution containing 5.6% of gold ammonium cyanide and having a hydrogen ion concentration adjusted to 8.5 was mixed with a stoppered plug.
The mixture was placed in a 300 ml Erlenmeyer flask, lightly stoppered, and placed in a 70 ° C water bath to perform an acceleration test. After 24 hours, a slight yellow precipitate was observed in the liquid in the container.

【0020】[0020]

【実施例3】シアン化金アンモニウム11.2%を含み、シ
アン化アンモニウムをそれぞれ0.005、0.03、 0.2、 1.
0%を含みさらに、水素イオン濃度 9.7に調整した溶液
を各々 100ml用意し、共栓式の 300mlの三角フラスコに
入れ、軽く栓をして70℃のウォーターバス中に入れて加
速試験をおこなった。24時間後も各々の容器内の液体に
変化は無かった。
Example 3 contains 11.2% of gold ammonium cyanide, and contains 0.005, 0.03, 0.2 and 1.
100% of each solution containing 0% and adjusted to a hydrogen ion concentration of 9.7 was prepared, placed in a stoppered 300 ml Erlenmeyer flask, lightly stoppered, and placed in a 70 ° C water bath to perform an acceleration test. . After 24 hours, there was no change in the liquid in each container.

【0021】[0021]

【発明の効果】以上のことから明らかなように本発明の
金メッキ用金塩溶液は、従来の金塩溶液のようにカリウ
ムの共析現象による金メッキの硬度上昇がなく、また時
間が経ってもブツやピンホールの発生原因となるシアン
金の沈殿がなく、接合性のよい柔らかな金メッキを得る
ことができると共に長期間の保存においても変質しない
効果がある。
As is clear from the above, the gold salt solution for gold plating of the present invention does not increase the hardness of the gold plating due to the eutectoid phenomenon of potassium, unlike the conventional gold salt solution. There is no precipitation of cyan gold, which causes the occurrence of bumps and pinholes, so that it is possible to obtain soft gold plating with good bonding properties, and there is an effect that there is no deterioration even during long-term storage.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C25D 3/48 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 7 , DB name) C25D 3/48

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 シアン化金アンモニウムを金塩としシア
ン化アンモニウムを0.005〜 1.0%を含みさらにアンモ
ニア水で水素イオン濃度8〜10のあいだに調整されてな
る金メッキ用金塩溶液。
1. A gold salt solution for gold plating, comprising gold cyanide as a gold salt, containing 0.005 to 1.0% of ammonium cyanide, and adjusted to a hydrogen ion concentration of 8 to 10 with aqueous ammonia.
JP03203897A 1991-07-18 1991-07-18 Gold salt solution for gold plating Expired - Lifetime JP3112513B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03203897A JP3112513B2 (en) 1991-07-18 1991-07-18 Gold salt solution for gold plating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03203897A JP3112513B2 (en) 1991-07-18 1991-07-18 Gold salt solution for gold plating

Publications (2)

Publication Number Publication Date
JPH0525678A JPH0525678A (en) 1993-02-02
JP3112513B2 true JP3112513B2 (en) 2000-11-27

Family

ID=16481530

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03203897A Expired - Lifetime JP3112513B2 (en) 1991-07-18 1991-07-18 Gold salt solution for gold plating

Country Status (1)

Country Link
JP (1) JP3112513B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4311689C2 (en) * 1993-04-08 1997-02-13 Roesler Roland Oberflaechen Centrifugal vibratory grinding machine with gap adjustment
JP2722324B2 (en) * 1994-01-13 1998-03-04 株式会社バンダイ Doll toy head rotation device
JP3433433B2 (en) * 1994-03-07 2003-08-04 矢崎総業株式会社 Shield connector
JP2804454B2 (en) * 1995-03-10 1998-09-24 株式会社バンダイ Doll toy head rotation device

Also Published As

Publication number Publication date
JPH0525678A (en) 1993-02-02

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