JP2833393B2 - Electroless copper plating method - Google Patents
Electroless copper plating methodInfo
- Publication number
- JP2833393B2 JP2833393B2 JP4344724A JP34472492A JP2833393B2 JP 2833393 B2 JP2833393 B2 JP 2833393B2 JP 4344724 A JP4344724 A JP 4344724A JP 34472492 A JP34472492 A JP 34472492A JP 2833393 B2 JP2833393 B2 JP 2833393B2
- Authority
- JP
- Japan
- Prior art keywords
- copper
- electroless
- solution
- tank
- electroless copper
- 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 - Fee Related
Links
Description
【0001】[0001]
【産業上の利用分野】本発明は、表面処理の分野で用い
られる無電解銅メッキに関し、具体的には、銅イオン、
銅イオンの錯化剤、銅イオンの還元剤、及びpH調整剤
を含有する無電解銅メッキ液を用いた無電解銅メッキ法
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to electroless copper plating used in the field of surface treatment.
The present invention relates to an electroless copper plating method using an electroless copper plating solution containing a copper ion complexing agent, a copper ion reducing agent, and a pH adjuster.
【0002】[0002]
【従来の技術】無電解メッキは被メッキ体の形状や材質
に制限を受けることなく被膜形成が可能で、量産性に富
む表面処理技術として益々脚光を浴びてきている。しか
し、この量産性を上げようとすると、メッキ液の補給が
問題となる。すなわち、無電解メッキの反応の進行に伴
い、メッキ液中に不足した金属イオンの補給は、従来金
属化合物を補給する形で行われている。しかし、この補
給した金属化合物は、メッキ液に存在する錯化剤と錯体
形成をする前にメッキ反応で発生する水素に還元され金
属化し、この金属化した粒子がメッキ液中に析出する。
又、補給した金属化合物はアルカリ性のメッキ液中で金
属水酸化物として沈澱物を生成し、この沈澱物が被メッ
キ体に金属とともに共析し、被メッキ体の表面に形成さ
れた金属被膜のザラツキ現象を起こす。さらに、上記現
象は浴負荷を大きくし、その結果金属イオンの消耗速度
の増大を招き、メッキ液を安定して使用できる可使時間
が短くなる。2. Description of the Related Art Electroless plating is capable of forming a film without being limited by the shape and material of a body to be plated, and is increasingly being spotlighted as a surface treatment technique which is rich in mass productivity. However, in order to increase the mass productivity, supply of the plating solution becomes a problem. That is, with the progress of the electroless plating reaction, the replenishment of the metal ions that are insufficient in the plating solution has conventionally been performed by replenishing the metal compound. However, the replenished metal compound is reduced to hydrogen generated by a plating reaction and metallized before forming a complex with a complexing agent present in the plating solution, and the metallized particles precipitate in the plating solution.
In addition, the replenished metal compound forms a precipitate as a metal hydroxide in an alkaline plating solution, and the precipitate co-deposits with the metal on the object to be plated to form a metal coating formed on the surface of the object to be plated. Produces a zaratsuki phenomenon. Further, the above phenomenon increases the bath load, resulting in an increase in the consumption rate of metal ions, and shortens the pot life in which the plating solution can be used stably.
【0003】[0003]
【発明が解決しようとする課題】本発明は上記の事実に
鑑みてなされたもので、その目的とするところは、補給
した金属イオンがメッキ液中に析出することもなく、且
つ長時間にわたり無電解メッキ液の活性を保持する無電
解銅メッキ法を提供することにある。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned circumstances, and has as its object to prevent the replenished metal ions from depositing in the plating solution and to maintain the metal ions free for a long time. An object of the present invention is to provide an electroless copper plating method that maintains the activity of an electrolytic plating solution.
【0004】[0004]
【課題を解決するための手段】本発明の無電解銅メッキ
法は、無電解銅メッキ槽内の銅イオン、銅イオンの錯化
剤、銅イオンの還元剤、及びpH調整剤を含有する無電
解銅メッキ液に上記銅イオンの補給を行うにあたって、
無電解銅メッキ槽内から一部取り出した無電解銅メッキ
液に、硫酸を添加し、上記銅イオンと銅イオンの錯化剤
が速やかに銅錯体を形成できるpH領域に調整する工
程、この状態の無電解銅メッキ液に新たに銅化合物を添
加し、銅錯体溶液を作製する工程、この銅錯体溶液を銅
錯体補給槽に貯蔵する工程、上記無電解銅メッキ液の測
定に応じて、上記銅錯体補給槽に貯蔵された銅錯体溶液
が補給される工程からなることを特徴とする。According to the present invention, there is provided an electroless copper plating method comprising a copper ion, a copper ion complexing agent, a copper ion reducing agent, and a pH adjuster in an electroless copper plating tank. When replenishing the above copper ions to the electrolytic copper plating solution,
Sulfuric acid is added to the electroless copper plating solution partially removed from the electroless copper plating bath to adjust the pH to a pH range where the complexing agent of copper ions and copper ions can quickly form a copper complex.
In this step, a copper compound is newly added to the electroless copper plating solution in this state, and a copper complex solution is prepared.
The method is characterized by comprising a step of storing in the complex replenishing tank and a step of replenishing the copper complex solution stored in the copper complex replenishing tank in accordance with the measurement of the electroless copper plating solution.
【0005】[0005]
【作用】本発明においては、メッキ液槽内の無電解銅メ
ッキ液に化学的に安定した状態の銅錯体溶液を補給する
ので銅粒子の析出もなく、銅水酸化物の沈澱物も生成し
ない。According to the present invention, no precipitation of copper particles since replenishing chemically stable state copper complex solution in an electroless copper main <br/> Tsu key solution in the plating solution tank, copper hydroxide Does not form.
【0006】以下、本発明に係る無電解銅メッキ法を図
面を参照しながら説明する。図1は本発明の一実施例に
係る無電解銅メッキ装置のブロック図である。Hereinafter, an electroless copper plating method according to the present invention will be described with reference to the drawings. FIG. 1 is a block diagram of an electroless copper plating apparatus according to one embodiment of the present invention.
【0007】図1に示す如く、無電解銅メッキ液槽1に
は、被メッキ体2にメッキを施すため無電解銅メッキ液
12が満たされている。この無電解銅メッキ液は主成分
として、銅イオン、銅イオンの錯化剤、銅イオンの還元
剤、及びpH調整剤を含有し、その他必要に応じて、界
面活性剤や安定剤等の添加剤を含む。上記メッキ液の温
度は一般に50℃〜90℃に保持される。As shown in FIG. 1, an electroless copper plating solution tank 1 is filled with an electroless copper plating solution 12 for plating an object 2 to be plated. As the electroless copper plating solution composed mainly complexing agent of copper ions, copper ions, a reducing agent of the copper ions, and contains a pH adjusting agent, other optionally added such as a surfactant and a stabilizer Agent. The temperature of the plating solution is generally maintained at 50 ° C to 90 ° C.
【0008】本発明では、銅錯体補給槽21に、銅イオ
ンとこの銅イオンの錯化剤とからなる銅錯体溶液7が貯
蔵されており、無電解銅メッキ液12中の銅イオンの消
費に伴い、無電解銅メッキ液槽1に補給される。上記銅
錯体溶液7の無電解銅メッキ液槽1への補給は間欠で行
われる。上記銅錯体溶液7は、無電解銅メッキ液12の
組成により適宜決定される。[0008] In the present invention, the copper complex replenishing tank 21, copper ions <br/> ting and copper complex solution 7 comprising a complexing agent of the copper ions are stored, in an electroless copper plating solution 12 As the copper ions are consumed, the electroless copper plating solution tank 1 is replenished. Line supply is intermittent for the electroless copper plating solution tank 1 of the copper <br/> complex solution 7
Will be The copper complex solution 7 is appropriately determined depending on the composition of the electroless copper plating solution 12.
【0009】上記無電解銅メッキの反応の進行に伴い、
銅イオンの還元剤8、pH調製剤9が適宜無電解銅メッ
キ液槽1に補給される。With the progress of the electroless copper plating reaction,
The copper ion reducing agent 8 and the pH adjusting agent 9 are appropriately replenished to the electroless copper plating solution tank 1.
【0010】上記銅錯体溶液7、pH調製剤9、及び銅
イオンの還元剤8は、無電解銅メッキ液槽1の無電解銅
メッキ液12をポンプ11でサンプリングし、銅イオン
濃度、還元剤の濃度、及びpH等の検出器を含むコント
ローラ3からの指示に基づき各銅錯体溶液7のポンプ
4、銅イオンの還元剤8のポンプ5、pH調製剤9のポ
ンプ6が作動し、自動的に補給が行われる。The above-mentioned copper complex solution 7, pH adjuster 9, and copper ion reducing agent 8 are sampled by a pump 11 from an electroless copper plating solution 12 in an electroless copper plating solution tank 1. A pump 4 for each copper complex solution 7, a pump 5 for a copper ion reducing agent 8, and a pH adjusting agent 9 based on instructions from the controller 3 including detectors such as a copper ion concentration, a reducing agent concentration, and a pH. The pump 6 operates, and replenishment is performed automatically.
【0011】本発明においては、メッキ反応の進行に応
じて、銅イオンと錯体を形成していた錯化剤が単独で存
在する錯化剤に戻ったメッキ液を無電解銅メッキ液槽1
からポンプ11を作動して一部取り出し、この取り出し
た液を錯化槽13へ送り、この錯化槽13に新たに銅化
合物17を添加して銅錯体溶液7とする。なお、錯化槽
13はスペアの錯化槽13aを設けておき、必要に応じ
て順次切り換える。In the present invention, as the plating reaction progresses, the plating solution in which the complexing agent which has formed a complex with copper ions returns to the complexing agent present alone is transferred to the electroless copper plating solution tank 1.
Extraction part by operating the pump 11 from, sends the extraction liquid to the complexing tank 13, the copper complex solution 7 newly adding copper of <br/> compound 17 in the complexation bath 13 . Note that the complexing tank 13 is provided with a spare complexing tank 13a, and is sequentially switched as necessary.
【0012】この銅錯体溶液7とするには、硫酸16を
供給し、銅化合物17、還元剤を添加して金属分の濃度
調整、還元剤の濃度調整を行う。硫酸でpH調整を先ず
行うのは、供給する銅イオンが錯化剤と速やかに銅錯体
を形成でき、化学的に安定した状態のpH領域にするた
めである。例えば、エチレンジアミン四酢酸を錯化剤と
して用いる無電解銅メッキ液の場合、pH4〜10の領
域で銅イオンが錯化剤と速やかに銅錯体を形成する。
又、必要に応じて銅イオンの錯化剤18と添加剤19を
添加し、これらの濃度調整を行って、上記銅錯体溶液7
とする。To prepare the copper complex solution 7, sulfuric acid 16 is supplied, and a copper compound 17 and a reducing agent are added to adjust the concentration of the metal component and the concentration of the reducing agent. The reason why the pH is first adjusted with sulfuric acid is that the supplied copper ions can quickly form a copper complex with the complexing agent, so that the pH range is in a chemically stable state . For example, in the case of an electroless copper plating solution using ethylenediaminetetraacetic acid as a complexing agent, copper ions quickly form a copper complex with the complexing agent in a pH range of 4 to 10.
Moreover, a complexing agent 18 and additives 19 of copper ions added as needed, perform these density adjustment, the copper complex solution 7
And
【0013】上記取り出した無電解銅メッキ液槽1の無
電解銅メッキ液12への銅化合物17の添加に際して
は、適宜に新しい銅錯体溶液7を混ぜて、無電解銅メッ
キ液12内の反応副生成物である蓄積塩が多くならない
ようにすることが好ましい。なお、電気透析法や逆浸透
法を用いて除去すると、無電解銅メッキ液12の不活性
の金属塩の濃度が増大するのを防ぐことができ好まし
い。[0013] Upon addition of the copper compound 17 to an electroless copper plating solution 12 in the electroless copper plating solution tank 1 taken out above is suitably mixed with new copper complex solution 7, electroless copper plating <br/> key It is preferable that the amount of the accumulated salt, which is a reaction by-product, in the liquid 12 is not increased. In addition, it is preferable to remove using an electrodialysis method or a reverse osmosis method because it is possible to prevent the concentration of the inert metal salt of the electroless copper plating solution 12 from increasing.
【0014】上記錯化槽13及びスペアの錯化槽13a
内の、銅化合物17を添加した銅錯体溶液7に、送風機
15より酸素を含む気体として空気を供給し、錯化槽1
3、及びスペアの錯化槽13a内に設けた散気管14か
ら微細分化した空気を供給して溶存させると、銅の析出
防止、及び攪拌として有効である。The complexing tank 13 and a spare complexing tank 13a
Air is supplied as a gas containing oxygen from a blower 15 to the copper complex solution 7 to which the copper compound 17 has been added.
3 and the supply and dissolution of finely divided air from the diffuser 14 provided in the spare complexing tank 13a is effective for preventing copper precipitation and stirring.
【0015】上記の如く変成された銅錯体溶液7はポン
プ20により銅錯体補給槽21に送られ、適宜無電解銅
メッキ液槽1に補給される。この補給する銅錯体溶液7
の温度は20℃以上から無電解銅メッキ液槽1内のメッ
キ液温迄の温度範囲にしておくと、無電解銅メッキ液槽
1内の温度分布を小さくするのに有効である。従って、
無電解銅メッキ液槽1へ銅錯体溶液7を補給する際、銅
錯体溶液7をヒータ10で加温しても良いし、銅錯体補
給槽21に保温装置を設けてもよい。The copper complex solution 7 modified as described above is sent to a copper complex replenishing tank 21 by a pump 20, and is appropriately replenished to the electroless copper plating solution tank 1. This replenished copper complex solution 7
The temperature to be effective to reduce electroless the copper keep the temperature range up to the plating solution temperature of the plating liquid tank 1, the temperature distribution of the electroless copper plating solution tank 1 from 20 ° C. or higher. Therefore,
When replenishing the copper complex solution 7 into an electroless copper plating solution tank 1, to the copper <br/> complex solution 7 may be heated by the heater 10 may be provided with a heat insulating device to the copper complex replenishing tank 21 .
【0016】[0016]
【実施例】実施例1 図1に示した無電解銅メッキ装置を使用して無電解銅メ
ッキを行った。無電解銅メッキ槽1内の無電解銅メッキ
液12は下記の条件のものを用いた。なお、この無電解
銅メッキ液12にpH調整剤9としてNaOHを加え
て、pHを測定したところpHは12.0であった。Example 1 Electroless copper plating was performed using the electroless copper plating apparatus shown in FIG. The electroless copper plating solution 12 in the electroless copper plating tank 1 used under the following conditions. In addition, NaOH was added as a pH adjuster 9 to the electroless copper plating solution 12, and the pH was measured. As a result, the pH was 12.0.
【0017】 無電解銅メッキ液の条件 ・CuSO4 5H2 O(金属イオン用)−−−− 10g/リットル ・EDTA2Na2H2 O (錯化剤)−−−− 30g/リットル ・HCHO(還元剤)−−−−−−−−−−− 1.8g/リットル ・シアン系添加剤(添加剤)−−−−−−−−−10mg/リットル ・ポリエチレングリコール(添加剤)−−−−200mg/リットル ・液温−−−−−−−−−−−−−−−−−−60℃ 容量360リットルの無電解銅メッキ液槽1に核付け処
理を施した処理面積2dm2 /リットルのガラスエポキ
シ基板を被メッキ体2とし、これを浸漬し無電解銅メッ
キを施した。無電解銅メッキ液槽1からメッキ液12の
試料をポンプ11を介してコントローラ3に送り、銅イ
オン濃度、還元剤の濃度、pHを測定し、各々の消耗量
に応じて、ポンプ4を作動させ補給用の銅錯体溶液7
を、ポンプ5を作動させ補給用の還元剤8であるHCH
Oを、ポンプ6を作動させ補給用のpH調整剤9である
NaOHを補給した。上記銅錯体溶液7は送液管の途中
にヒータ10を設け、液温40℃で補給した。Conditions for electroless copper plating solution CuSO 4 5H 2 O (for metal ions) 10 g / l EDTA 2 Na 2 H 2 O (complexing agent) 30 g / l HCHO (reducing agent) 1.8 g / l Cyanide additive (additive) 10 mg / l Polyethylene glycol (additive) 200 mg / l 1 liter ・ Liquid temperature------------------------60 ° C. A glass with a processing area of 2 dm 2 / l in which a nucleation treatment is applied to a 360-liter electroless copper plating bath 1 The epoxy substrate was used as the plating object 2, which was immersed and subjected to electroless copper plating. Feed from an electroless copper plating solution tank 1 a sample of the plating solution 12 to the controller 3 via the pump 11, the copper Lee <br/> on concentration, the concentration of the reducing agent, to measure the pH, depending on the respective consumption , Pump 4 is activated to supply copper complex solution 7
And HCH, which is a replenishing reducing agent 8 by operating the pump 5
O was supplied with NaOH as a pH adjuster 9 for supply by operating the pump 6. The copper complex solution 7 was supplied at a liquid temperature of 40 ° C. by providing a heater 10 in the middle of the liquid sending pipe.
【0018】メッキ反応の進行に応じて、ポンプ11を
作動し、無電解銅メッキ液槽1内の無電解銅メッキ12
を一部取り出し、容量が150リットルの錯化槽13に
送った。なおスペアの槽13aを設けておき、必要に応
じて順次切り換えることとした。The pump 11 is operated in accordance with the progress of the plating reaction, and the electroless copper plating 12 in the electroless copper plating solution tank 1 is operated.
Was partially taken out and sent to a complexing tank 13 having a capacity of 150 liters. It is to be noted that a spare tank 13a is provided, and switching is sequentially performed as necessary.
【0019】上記取り出した液は先ず硫酸16によりp
Hを10.5に調整した後、還元剤を含んだ銅化合物1
7の水溶液、硫酸銅が250g/リットルとHCHOが
48g/リットルの割合の混合溶液を添加し、銅濃度が
20g/リットルと成るよう調製した。pH10.5
で、速やかに銅とEDTAの金属錯体を生成した。その
後、銅イオンの錯化剤18として、EDTAのアルカリ
溶液を、添加剤19としてシアン系添加剤、ポリエチレ
ングリコールを添加し、下記組成表に示す銅錯体溶液7
に調製した。The removed liquid is first p-pulped with sulfuric acid 16
After adjusting H to 10.5, copper compound 1 containing a reducing agent
An aqueous solution of No. 7 and a mixed solution of copper sulfate at 250 g / L and HCHO at 48 g / L were added to adjust the copper concentration to 20 g / L. pH 10.5
As a result, a metal complex of copper and EDTA was quickly formed. Thereafter, an alkali solution of EDTA was added as a complexing agent 18 for copper ions, and a cyanide additive and polyethylene glycol were added as additives 19, and a copper complex solution 7 shown in the following composition table was added.
Was prepared.
【0020】 銅錯体溶液の組成 ・CuSO4 5H2 O(金属イオン用)−−−− 20g/リットル ・EDTA2Na2H2 O (錯化剤)−−−− 30g/リットル ・HCHO(還元剤)−−−−−−−−−−− 3.6g/リットル ・シアン系添加剤(添加剤)−−−−−−−−−10mg/リットル ・ポリエチレングリコール(添加剤)−−−−200mg/リットル ・pH−−−−−−−−−−−−−−−−−−−10.5 上記錯化槽13、及びスペアの錯化槽13a内の、銅化
合物17を添加した銅錯体溶液7に、送風機15より酸
素を含む気体として空気を供給し、錯化槽13、及びス
ペアの錯化槽13a内に設けた散気管14から微細分化
した空気を供給した。この銅化合物17が添加した銅錯
体溶液7はポンプ20を介して銅錯体補給槽21へ送
り、補給用の銅錯体溶液7として利用した。Composition of copper complex solution CuSO 4 5H 2 O (for metal ions) 20 g / liter EDTA 2 Na 2 H 2 O (complexing agent) 30 g / liter HCHO (reducing agent) −−−−−−−−− 3.6 g / l ・ Cyanide-based additive (additive) -10-mg / l ・ Polyethylene glycol (additive) ----- 200 mg / l ・pH ------------------- 10.5 the complexing tank 13, and the spare complexing tank 13a, adding copper of <br/> compound 17 Air was supplied from the blower 15 to the copper complex solution 7 as a gas containing oxygen, and finely divided air was supplied from the diffuser 14 provided in the complexing bath 13 and the spare complexing bath 13a. The copper compound 17 copper complexing <br/> body solution 7 was added through the pump 20 feeding to the copper complex replenishing tank 21, was utilized as the copper complex solution 7 for supplementation.
【0021】上述の操作で無電解銅メッキを5ターンま
で継続したが、銅がメッキ液槽1内に析出することもな
く被メッキ体2の表面に形成した銅メッキ被膜はザラツ
キ現象もなく良好であった。Although the electroless copper plating was continued up to 5 turns by the above operation, the copper plating film formed on the surface of the plating object 2 without copper being deposited in the plating solution tank 1 was good without any roughness phenomenon. Met.
【0022】比較例実施例1の銅錯体溶液に代えて、下
記条件の銅イオン補給液を用い、メッキ液槽に補給した
以外は実施例1と同様の無電解銅メッキ液を用いメッキ
を行った。COMPARATIVE EXAMPLE Plating was performed using the same electroless copper plating solution as in Example 1 except that a copper ion replenishing solution under the following conditions was used in place of the copper complex solution of Example 1 and replenished to the plating solution tank. Was.
【0023】 銅イオン補給液の条件 ・CuSO4 5H2 O−−−−−−−−−−−−125g/リットル ・HCHO−−−−−−−−−−−−−−−− 27g/リットル ・pH−−−−−−−−−−−−−−−−− pHを3とする量 ・液の温度−−−−−−−−−−−−−−−− 40℃ その結果、1タ−ン終了後にメッキ液槽の底に銅が析出
し、8時間後にはメッキ液の交換が必要となった。Conditions for the copper ion replenishing liquid ・ CuSO 4 5H 2 O --- 125 g / liter ・ HCHO -------------------------- 27 g / 1 liter ・ pH -------------------------------- Amount to adjust the pH to 3 -Temperature of the liquid --40--40 ℃ After one turn, copper was deposited on the bottom of the plating solution tank, and after 8 hours, the plating solution had to be replaced.
【0024】[0024]
【発明の効果】本発明の無電解銅メッキ法は、化学的に
安定な、銅イオンと上記銅イオンの錯化剤とからなる銅
錯体溶液を用いることにより、補給した銅イオンがメッ
キ液中に析出することもない。且つ、この銅錯体溶液
は、無電解メッキ液槽内から取り出した無電解銅メッキ
液に、硫酸を添加し、上記銅イオンと銅イオンの錯化剤
が速やかに銅錯体を形成できるpH領域に調整し、銅化
合物を添加し作製するので、長時間にわたり無電解銅メ
ッキ液の活性を保持する。Electroless copper plating method of the present invention exhibits, chemically stable, by using copper <br/> complex solution consisting of a complexing agent of copper ions and the copper ions, supplemented with copper ions Does not precipitate in the plating solution. And this copper complex solution
It is in an electroless copper plating solution taken out from the electroless plating solution bath, was added sulfuric acid, complexing agent of the copper ions and copper ions
Promptly adjusted to pH region capable of forming a copper complex, since the addition of copper reduction <br/> compound is prepared to hold the electroless copper main <br/> Tsu liquid activity over time.
【図1】本発明の一実施例に係る無電解銅メッキ装置の
ブロック図である。FIG. 1 is a block diagram of an electroless copper plating apparatus according to one embodiment of the present invention.
1 無電解銅メッキ液槽 2 被メッキ体 3 コントローラ 4 ポンプ 5 ポンプ 6 ポンプ 7 銅錯体溶液 8 還元剤 9 pH調整剤 10 ヒータ 11 ポンプ 12 無電解銅メッキ液 13 錯化槽 13a 錯化槽 14 散気管 15 送風機 16 硫酸 17 銅化合物 18 錯化剤 19 添加剤 20 ポンプ 21 銅錯体補給槽DESCRIPTION OF SYMBOLS 1 Electroless copper plating liquid tank 2 Plated object 3 Controller 4 Pump 5 Pump 6 Pump 7 Copper complex solution 8 Reducing agent 9 pH adjuster 10 Heater 11 Pump 12 Electroless copper plating liquid 13 Complexing tank 13a Complexing tank 14 Dispersion Trachea 15 Blower 16 Sulfate 17 Copper compound 18 Complexing agent 19 Additive 20 Pump 21 Copper complex supply tank
───────────────────────────────────────────────────── フロントページの続き (72)発明者 服部 浩昌 大阪府門真市大字門真1048番地松下電工 株式会社内 (72)発明者 高橋 広明 大阪府門真市大字門真1048番地松下電工 株式会社内 (56)参考文献 特開 平3−75378(JP,A) 特開 平2−298273(JP,A) 特公 平1−49787(JP,B2) (58)調査した分野(Int.Cl.6,DB名) C23C 18/40 C23C 18/31──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Hiromasa Hattori 1048 Kadoma Kadoma, Osaka Prefecture Matsushita Electric Works, Ltd. References JP-A-3-75378 (JP, A) JP-A-2-298273 (JP, A) JP-A-1-49787 (JP, B2) (58) Fields investigated (Int. Cl. 6 , DB name ) C23C 18/40 C23C 18/31
Claims (1)
ンの錯化剤、銅イオンの還元剤、及びpH調整剤を含有
する無電解銅メッキ液に上記銅イオンの補給を行うにあ
たって、 無電解銅メッキ槽内から一部取り出した無電解銅メッキ
液に、硫酸を添加し、上記銅イオンと銅イオンの錯化剤
が速やかに銅錯体を形成できるpH領域に調整する工
程、 この状態の無電解銅メッキ液 に新たに銅化合物を添加
し、銅錯体溶液を作製する工程、 この銅錯体溶液を銅錯体補給槽に貯蔵する工程、 上記無電解銅メッキ液の測定に応じて、上記銅錯体補給
槽に貯蔵された銅錯体溶液が補給される工程からなるこ
とを特徴とする無電解銅メッキ法。1. A copper ions electroless copper plating bath, a complexing agent of copper ions <br/> down, the copper ion reducing agent, and the copper ion in an electroless copper plating solution containing a pH adjusting agent When replenishing, sulfuric acid is added to the electroless copper plating solution partially removed from the electroless copper plating tank, and adjusted to a pH range where the above-mentioned complexing agent of copper ions and copper ions can quickly form a copper complex. Work
In this state, a copper compound is newly added to the electroless copper plating solution in this state , a copper complex solution is prepared, a copper complex solution is stored in a copper complex replenishing tank, and the above electroless copper plating solution is measured. If necessary, replenish the above copper complex
An electroless copper plating method comprising a step of replenishing a copper complex solution stored in a tank .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4344724A JP2833393B2 (en) | 1992-12-24 | 1992-12-24 | Electroless copper plating method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4344724A JP2833393B2 (en) | 1992-12-24 | 1992-12-24 | Electroless copper plating method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06280033A JPH06280033A (en) | 1994-10-04 |
JP2833393B2 true JP2833393B2 (en) | 1998-12-09 |
Family
ID=18371492
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4344724A Expired - Fee Related JP2833393B2 (en) | 1992-12-24 | 1992-12-24 | Electroless copper plating method |
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JP (1) | JP2833393B2 (en) |
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JP3985864B2 (en) * | 2002-08-27 | 2007-10-03 | 株式会社荏原製作所 | Electroless plating apparatus and method |
CN110234203A (en) * | 2019-06-17 | 2019-09-13 | 广州兴森快捷电路科技有限公司 | A kind of heavy silver-colored production line of PCB, heavy silver-colored liquid medicine supply control system and its method |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS6449787A (en) * | 1987-08-20 | 1989-02-27 | Okuchi Kensan Kk | Flat seamed pipe |
JPH02298273A (en) * | 1989-05-10 | 1990-12-10 | Hitachi Aic Inc | Mixer for electroless plating solution |
JPH0375378A (en) * | 1990-03-06 | 1991-03-29 | Purantetsukusu:Kk | Circulating device for plating solution in electroless plating bath |
-
1992
- 1992-12-24 JP JP4344724A patent/JP2833393B2/en not_active Expired - Fee Related
Also Published As
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