JPH0633250A - System for automatically controlling copper electroless-plating bath - Google Patents

System for automatically controlling copper electroless-plating bath

Info

Publication number
JPH0633250A
JPH0633250A JP19363492A JP19363492A JPH0633250A JP H0633250 A JPH0633250 A JP H0633250A JP 19363492 A JP19363492 A JP 19363492A JP 19363492 A JP19363492 A JP 19363492A JP H0633250 A JPH0633250 A JP H0633250A
Authority
JP
Japan
Prior art keywords
copper plating
copper
plating
plating solution
concentration
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
JP19363492A
Other languages
Japanese (ja)
Inventor
Hiroko Nakai
裕子 中井
Hideki Shibuya
秀樹 渋谷
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 Chemi Con Corp
Original Assignee
Nippon Chemi Con 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 Nippon Chemi Con Corp filed Critical Nippon Chemi Con Corp
Priority to JP19363492A priority Critical patent/JPH0633250A/en
Publication of JPH0633250A publication Critical patent/JPH0633250A/en
Pending legal-status Critical Current

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  • Chemically Coating (AREA)

Abstract

PURPOSE:To form a high-quality copper plating film and to prolong the service life of a plating soln. by increasing the plating soln. component concn. at the start of plating in the Cu electroless plating and then controlling the component concn. to a preset value. CONSTITUTION:CuSO4 is used as a Cu salt, formaldehyde as the reducing agent for Cu ion and NaOH as the pH regulator in the Cu electroless-plating solution to plate a material with copper. In this case, the concns. of the Cu salt, reducing agent, pH regulator, etc., are increased at the start of plating, and then gradually decreased to the preset values according to the decrease of each component concentration. Consequently, a defective Cu plating film due to the abnormal deposition of Cu is not formed, and the service life of the plating soln. is prolonged since the plating soln. is not decomposed.

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、無電解銅めっき浴を自
動管理するシステムに関し、特に銅めっき液中の各成分
濃度を銅めっき反応中に変化させて、良好な品質の製品
を得ることができる無電解銅めっき浴自動管理システム
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a system for automatically controlling an electroless copper plating bath, and in particular, to obtain a product of good quality by changing the concentration of each component in a copper plating solution during a copper plating reaction. The present invention relates to an electroless copper plating bath automatic management system capable of performing.

【0002】[0002]

【従来の技術】無電解めっき法は、電解めっき法に比較
して、被めっき体をめっき液に接するのみで、すべての
部位に均一な厚さの被覆が得られ、かつ析出物の硬度が
高いなどの特徴がある。そのためには、銅めっき液を適
切に管理する必要がある。
2. Description of the Related Art The electroless plating method, as compared with the electrolytic plating method, can obtain a coating of uniform thickness on all parts by simply contacting the object to be plated with a plating solution and the hardness of precipitates. There are features such as high price. For that purpose, it is necessary to appropriately manage the copper plating solution.

【0003】従来、無電解銅めっき液の管理は、銅めっ
き液の管理に必要な項目である、例えば銅濃度、還元剤
濃度、pH値を各々経時的に測定し、予め設定した管理
値より低くなつた場合、補充液を添加して各成分濃度を
管理値に調整しながら銅めっき反応を継続する。通常、
予め設定した各成分濃度の管理値は、銅めっき反応の開
始から終了時まで変更させない。
Conventionally, the control of the electroless copper plating solution is an item necessary for the control of the copper plating solution. For example, the copper concentration, the reducing agent concentration, and the pH value are measured with time, and the control values are set in advance. When the temperature becomes low, the copper plating reaction is continued while adding the replenishing solution and adjusting the concentration of each component to the control value. Normal,
The preset control value of each component concentration is not changed from the start to the end of the copper plating reaction.

【0004】[0004]

【発明が解決しようとする課題】一般的に、銅めっき反
応を開始させるためには、各成分濃度の高い高反応性の
銅めっき液が要求される。一方、銅めっき反応を定常的
に持続させるために要求される銅めっき液濃度は、銅め
っき反応の開始時の濃度よりも低いのが通常である。銅
めっき液中の各成分濃度を反応開始時の高い濃度のまま
銅めっき反応を継続すると、銅めっき液の分解および異
常析出が発生する。
Generally, in order to start the copper plating reaction, a highly reactive copper plating solution having a high concentration of each component is required. On the other hand, the concentration of the copper plating solution required to constantly maintain the copper plating reaction is usually lower than the concentration at the start of the copper plating reaction. If the copper plating reaction is continued while the concentration of each component in the copper plating solution remains high at the start of the reaction, decomposition and abnormal deposition of the copper plating solution will occur.

【0005】本発明の目的は、銅めっき反応を速やかに
開始せしめ、かつ銅めっき反応中に銅めっき液の分解お
よび異常析出などが発生しない自動管理システムを提供
することにある。
It is an object of the present invention to provide an automatic management system that promptly starts a copper plating reaction and does not cause decomposition or abnormal deposition of a copper plating solution during the copper plating reaction.

【0006】[0006]

【課題を解決するための手段】本発明に係る無電解銅め
っき浴自動管理システムは、銅塩、還元剤、pH調整剤
からなる無電解銅めっき液の所定量をめっき液槽に充填
し、このめっき液槽内の前記銅めっき液に対してそれぞ
れ成分濃度を分析し、各成分が予め設定した管理値より
低下した際に、必要な成分の補充を行うよう構成した無
電解銅めっき浴自動管理システムにおいて、銅めっき反
応の出発時において各成分濃度の管理値を高く設定し、
銅めっき反応が開始した後は、予め設定した各成分濃度
の管理値に変化させることを特徴とする。
The electroless copper plating bath automatic management system according to the present invention is a plating solution tank filled with a predetermined amount of an electroless copper plating solution consisting of a copper salt, a reducing agent and a pH adjusting agent, An automatic electroless copper plating bath configured to analyze the component concentrations of the copper plating solution in the plating solution tank and replenish the necessary components when each component falls below a preset control value. In the control system, the control value of each component concentration is set high at the start of the copper plating reaction,
After the copper plating reaction is started, the control value of each component concentration is changed to a preset value.

【0007】前記の無電解銅めっき浴自動管理システム
において、好適には、銅塩は硫酸銅溶液であり、還元剤
はホルムアルデヒド溶液であり、pH調整剤は水酸化ナ
トリウム溶液である。
In the above electroless copper plating bath automatic control system, preferably, the copper salt is a copper sulfate solution, the reducing agent is a formaldehyde solution, and the pH adjusting agent is a sodium hydroxide solution.

【0008】[0008]

【作用】銅めっき液の管理項目は銅濃度、ホルムアルデ
ヒド濃度、pH値である。銅めっき液の液管理は、各成
分濃度を銅めっき反応中に経時的に測定して、予め設定
した管理値より濃度が低くなつた場合に補充液を添加し
て、銅めっき液を一定状態に保持する方法で行う。
[Function] The control items of the copper plating solution are copper concentration, formaldehyde concentration, and pH value. Liquid management of the copper plating solution is to measure each component concentration over time during the copper plating reaction, and when the concentration becomes lower than the preset control value, add a replenishing solution to keep the copper plating solution in a constant state. To hold in.

【0009】この各成分濃度の管理値について、銅めっ
き反応を開始させるためには、各成分濃度の高い銅めっ
き液を使用する。このことによつて銅めっき反応が速や
かにスタートする。銅めっき反応がスタートした後は、
予め設定した各成分濃度の管理値に切替えて銅めっき反
応を継続して、銅めっき製品を得る。この方法によつ
て、銅めっき反応中の異常析出および分解などの発生を
防ぐことができる。その結果、銅めっき製品は良好な品
質を有し、銅めっき液は高寿命で使用することができ
る。
With respect to the control value of each component concentration, a copper plating solution having a high concentration of each component is used to start the copper plating reaction. This promptly starts the copper plating reaction. After the copper plating reaction starts,
The copper plating reaction is continued by switching to the preset control value of each component concentration to obtain a copper plated product. This method can prevent the occurrence of abnormal deposition and decomposition during the copper plating reaction. As a result, the copper-plated product has good quality, and the copper-plating solution can be used with a long life.

【0010】[0010]

【実施例】次に、本発明に係る無電解銅めっき浴自動管
理システムの実施例につき、添付図面を参照しながら以
下詳細に説明する。
EXAMPLES Examples of the electroless copper plating bath automatic control system according to the present invention will be described below in detail with reference to the accompanying drawings.

【0011】実施例 硫酸銅(5水和物)100g、ホルムアルデヒド(37
%水溶液として)32mlを10リットルの水に溶解
し、1mol/l水酸化ナトリウム溶液でpH12.6
に調節して、銅めっき液10リットルを調製して使用し
た。この銅めっき液の各成分濃度は、銅:2.6g/リ
ットル、ホルムアルデヒド:0.04モル/リットル、
pH:12.6であつた。
Example 100 g of copper sulfate (pentahydrate), formaldehyde (37
% Water solution) in 10 liters of water and pH 12.6 with 1 mol / l sodium hydroxide solution.
Then, 10 liters of the copper plating solution was prepared and used. The concentration of each component of this copper plating solution was as follows: copper: 2.6 g / liter, formaldehyde: 0.04 mol / liter,
The pH was 12.6.

【0012】銅めっき反応は70℃で行い、被めっき試
料としてエポキシ銅張積層板を使用した。
The copper plating reaction was carried out at 70 ° C., and an epoxy copper clad laminate was used as a sample to be plated.

【0013】銅めっ反応が進行するに従い、図1に示す
ように銅濃度が減少して管理値下限に接近した。63g
/l硫酸銅溶液を補充添加して、銅濃度を管理値上限に
まで上昇させた。銅めっき反応が速やかにスタートし、
その後図1に示すように管理値を低く変更して、銅:
2.4g/リットル、ホルムアルデヒド:0.027モ
ル/リットル、pH:12.4とした。次いで、上記の
硫酸銅溶液の補充を反復して、銅濃度を管理限界範囲内
に保持しつつ銅めっき反応を継続した。
As the copper plating reaction proceeded, the copper concentration decreased and approached the lower limit of the control value as shown in FIG. 63 g
/ L copper sulphate solution was replenished and added to raise the copper concentration to the upper limit of the control value. The copper plating reaction starts quickly,
After that, the control value was changed to a lower value as shown in Fig. 1, and copper:
The amount was 2.4 g / liter, formaldehyde was 0.027 mol / liter, and pH was 12.4. Then, the above copper sulfate solution was replenished repeatedly to continue the copper plating reaction while keeping the copper concentration within the control limit range.

【0014】この間、銅の析出は正常に進行し、銅めっ
き液の異常な分解は見られなかつた。その結果、得られ
た銅めっき体は、良好な銅めっき被膜を有した。また、
銅めっき液は比較的長期間使用することができた。
During this time, copper deposition proceeded normally, and no abnormal decomposition of the copper plating solution was observed. As a result, the obtained copper plated body had a good copper plating film. Also,
The copper plating solution could be used for a relatively long period of time.

【0015】比較例 硫酸銅(5水和物)100g、ホルムアルデヒド(37
%水溶液として)32mlを10リットルの水に溶解
し、1mol/l水酸化ナトリウム溶液でpH12.6
に調節して、銅めっき液10リットルを調製して使用し
た。この銅めっき液の各成分濃度は、銅:2.6g/リ
ットル、ホルムアルデヒド:0.04モル/リットル、
pH:12.6であつた。
Comparative Example 100 g of copper sulfate (pentahydrate), formaldehyde (37
% Water solution) in 10 liters of water and pH 12.6 with 1 mol / l sodium hydroxide solution.
Then, 10 liters of the copper plating solution was prepared and used. The concentration of each component of this copper plating solution was as follows: copper: 2.6 g / liter, formaldehyde: 0.04 mol / liter,
The pH was 12.6.

【0016】銅めっき反応は70℃で行い、被めっき試
料としてエポキシ銅張積層板を使用した。
The copper plating reaction was carried out at 70 ° C., and an epoxy copper clad laminate was used as a sample to be plated.

【0017】銅めっ反応が進行するに従い、図2に示す
ように銅濃度が減少して管理値下限に接近した。63g
/l硫酸銅溶液を補充添加して、銅濃度を管理値上限に
まで上昇させた。銅めっき反応が速やかにスタートし
た。その後も、管理値を変更せずに硫酸銅溶液の補充を
反復して、銅濃度を管理限界範囲内に保持しつつ銅めっ
き反応を継続した。
As the copper plating reaction progressed, the copper concentration decreased as shown in FIG. 2 and approached the lower limit of the control value. 63 g
/ L copper sulphate solution was replenished and added to raise the copper concentration to the upper limit of the control value. The copper plating reaction started quickly. After that, replenishment of the copper sulfate solution was repeated without changing the control value, and the copper plating reaction was continued while keeping the copper concentration within the control limit range.

【0018】この間、銅の異常析出が発生し、また銅め
っき液の分解も見られた。その結果、得られた銅めっき
体は、銅めっき被膜が不良であつた。また、銅めっき液
の寿命が短期であつた。
During this time, abnormal precipitation of copper occurred and decomposition of the copper plating solution was also observed. As a result, the obtained copper-plated body had a poor copper-plated coating. In addition, the life of the copper plating solution was short.

【0019】[0019]

【発明の効果】前述したように、本発明によれば、銅め
っき反応の出発時には各成分濃度の管理値を高く設定
し、銅めっき反応が開始した後は、管理値を低く変化さ
せることによつて、銅めっき液の分解および異常析出を
防止することができた。その結果、銅めっき製品の品質
が確保され、かつ銅めっき液の高寿命化が達成された。
As described above, according to the present invention, the control value of each component concentration is set to a high value at the start of the copper plating reaction, and the control value is changed to a low value after the copper plating reaction starts. Therefore, the decomposition and abnormal deposition of the copper plating solution could be prevented. As a result, the quality of the copper-plated product was ensured and the life of the copper-plating solution was extended.

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

【図1】本発明に係る無電解銅めっき浴自動管理システ
ムによる銅めっき液の銅濃度管理状態の実施例を示す説
明図である。
FIG. 1 is an explanatory diagram showing an example of a copper concentration control state of a copper plating solution by an electroless copper plating bath automatic control system according to the present invention.

【図2】従来の無電解銅めっき浴自動管理システムによ
る銅めっき液の銅濃度管理状態の比較例を示す説明図で
ある。
FIG. 2 is an explanatory view showing a comparative example of a copper concentration control state of a copper plating solution by a conventional electroless copper plating bath automatic control system.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 銅塩、還元剤、pH調整剤からなる無電
解銅めっき液の所定量をめっき液槽に充填し、このめっ
き液槽内の前記銅めっき液に対してそれぞれ成分濃度を
分析し、各成分が予め設定した管理値より低下した際
に、必要な成分の補充を行うよう構成した無電解銅めっ
き浴自動管理システムにおいて、銅めっき反応の出発時
において各成分濃度の管理値を高く設定し、銅めっき反
応が開始した後は、予め設定した各成分濃度の管理値に
変化させることを特徴とする無電解銅めっき浴自動管理
システム
1. A plating solution tank is filled with a predetermined amount of an electroless copper plating solution comprising a copper salt, a reducing agent, and a pH adjusting agent, and the component concentrations of the copper plating solution in the plating solution tank are analyzed. However, in the automatic electroless copper plating bath management system configured to replenish necessary components when each component falls below the preset control value, the control value of each component concentration is set at the start of the copper plating reaction. After the copper plating reaction is set to a high value, the automatic control system for electroless copper plating bath is characterized in that the control value of each component concentration is changed to a preset value.
【請求項2】 銅塩が硫酸銅であり、還元剤がホルムア
ルデヒドであり、pH調整剤が水酸化ナトリウムである
請求項1記載の無電解銅めっき浴自動管理システム。
2. The electroless copper plating bath automatic management system according to claim 1, wherein the copper salt is copper sulfate, the reducing agent is formaldehyde, and the pH adjuster is sodium hydroxide.
JP19363492A 1992-07-21 1992-07-21 System for automatically controlling copper electroless-plating bath Pending JPH0633250A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19363492A JPH0633250A (en) 1992-07-21 1992-07-21 System for automatically controlling copper electroless-plating bath

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19363492A JPH0633250A (en) 1992-07-21 1992-07-21 System for automatically controlling copper electroless-plating bath

Publications (1)

Publication Number Publication Date
JPH0633250A true JPH0633250A (en) 1994-02-08

Family

ID=16311211

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19363492A Pending JPH0633250A (en) 1992-07-21 1992-07-21 System for automatically controlling copper electroless-plating bath

Country Status (1)

Country Link
JP (1) JPH0633250A (en)

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