JPH04187800A - Method for controlling copper sulfate plating bath - Google Patents

Method for controlling copper sulfate plating bath

Info

Publication number
JPH04187800A
JPH04187800A JP31535890A JP31535890A JPH04187800A JP H04187800 A JPH04187800 A JP H04187800A JP 31535890 A JP31535890 A JP 31535890A JP 31535890 A JP31535890 A JP 31535890A JP H04187800 A JPH04187800 A JP H04187800A
Authority
JP
Japan
Prior art keywords
additive
plating
bath
copper sulfate
tank
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.)
Granted
Application number
JP31535890A
Other languages
Japanese (ja)
Other versions
JP2558388B2 (en
Inventor
Shigeki Nakajima
茂樹 中島
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.)
NEC Toppan Circuit Solutions Toyama Inc
Original Assignee
NEC Toppan Circuit Solutions Toyama Inc
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 NEC Toppan Circuit Solutions Toyama Inc filed Critical NEC Toppan Circuit Solutions Toyama Inc
Priority to JP2315358A priority Critical patent/JP2558388B2/en
Publication of JPH04187800A publication Critical patent/JPH04187800A/en
Application granted granted Critical
Publication of JP2558388B2 publication Critical patent/JP2558388B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Electroplating And Plating Baths Therefor (AREA)

Abstract

PURPOSE:To keep the stability of a copper sulfate plating bath and to prevent defective plating by determining the concn. of an additive in the bath, calculating a deficient amount in the additive from the result, replenishing the deficient amount and further filtering off the by-product by activated carbon. CONSTITUTION:A fixed amt. of the plating soln. is sampled from a copper sulfate plating tank 1 and sent to an automatic additive analyzer 2. The additive concn. in the plating soln. is determined by the potential-scanning stripping method using a rotary electrode. A deficiency in the additive is calculated by a controller 3 from the additive concn. The deficiency is replenished to the tank 1 from an additive tank 4a through a fixed delivery pump 4. An activated-carbon filtration circulating pump 6 is operated in accordance with the integrated supply of the additive to circulate the plating soln. through an activated-carbon tank filter 5, and the by-product in the plating bath is filtered off by the activated carbon. Consequently, the additive concn. in the bath is kept in a specified range, the stability of the bath is maintained, and defective plating is prevented.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は硫酸銅めっき浴の管理方法に関し、特に添加剤
の管理方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for managing a copper sulfate plating bath, and particularly to a method for managing additives.

〔従来の技術〕[Conventional technology]

硫酸銅めっき浴は、基本的に銅イオン、硫酸、塩素イオ
ン、添加剤などで構成されている。この内、硫酸、塩素
イオンは、めっき反応によって濃度が低下する因子であ
り、銅イオンは、めっき反応と共に濃度が増加する。こ
れら因子の過不足は、めっき均一性やめっき仕上りを悪
化する為、硫酸は中和滴定法、塩素イオン、銅イオンは
比色法により自動分析管理をし、増加する銅イオンにつ
いては弱電解法により過剰銅イオンを金属銅として析出
させ銅イオン濃度を一定にしていた。−方、添加剤は、
めっき反応により消耗されその副生成物を生じる。添加
剤濃度不足及び副生成物の増加は、めっき仕上りやめっ
き物性等に最も強く影響する為、添加剤の濃度管理は重
要である。しかし、硫酸銅めっき浴中の添加剤の含有量
は、微量であり定量分析が大変困難であった為、−船釣
には分析せずに硫酸銅めっきの積算印加電流値に基づき
補充するか、ハルセル試験等の仕上り状態により補充を
行っていた。
A copper sulfate plating bath basically consists of copper ions, sulfuric acid, chloride ions, additives, etc. Among these, sulfuric acid and chloride ions are factors whose concentration decreases with the plating reaction, and the concentration of copper ion increases with the plating reaction. Excess or deficiency of these factors will deteriorate plating uniformity and plating finish, so sulfuric acid is automatically analyzed using neutralization titration, chlorine ions and copper ions are analyzed using colorimetry, and increased copper ions are analyzed using weak electrolytic method. Excess copper ions were precipitated as metallic copper to keep the copper ion concentration constant. - On the other hand, the additive is
It is consumed by the plating reaction and produces its by-products. Insufficient additive concentration and increase in by-products have the strongest effect on plating finish, plating physical properties, etc., so controlling the concentration of additives is important. However, the content of additives in the copper sulfate plating bath was very small and quantitative analysis was very difficult. , replenishment was carried out depending on the finished state of the Hull cell test, etc.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

従来の管理方法では、硫酸銅めっき浴中の添加剤濃度を
定量分析できず、めっき仕上りや物性を一定に保つこと
が困難であり、添加剤濃度が下限濃度以下になるとめっ
き仕上り不良や、物性不良を引き起こすという問題があ
った、 本発明の目的は、かかる従来欠点を解決し、硫酸銅めっ
き浴の添加剤濃度を一定範囲に維持することができ、そ
の結果めっき浴の安定性が保たれ、めっき仕上り不良を
防止でき、そして一定の硫酸銅めっき物性が維持てきる
硫酸鋼めっき浴の管理方法を提供することにある。
With conventional control methods, it is not possible to quantitatively analyze the additive concentration in the copper sulfate plating bath, making it difficult to maintain a constant plating finish and physical properties.If the additive concentration falls below the lower limit concentration, poor plating finish or physical properties may occur. The object of the present invention is to solve the conventional drawbacks and to maintain the additive concentration in a copper sulfate plating bath within a certain range, thereby maintaining the stability of the plating bath. An object of the present invention is to provide a method for managing a sulfuric acid steel plating bath that can prevent poor plating finish and maintain constant physical properties of copper sulfate plating.

〔課題を解決するための手段〕[Means to solve the problem]

本発明の硫酸銅めっき浴の管理方法は、硫酸銅めっき槽
から一定量のめっき液をサンプリングする工程と、回転
電極を用いた電位走査ストリッピング法により前記サン
プリング液中の添加剤濃度を定量する工程と、その添加
剤濃度から不足する添加材料を演算する工程と、不足す
る添加剤を補充する工程と、添加剤の積算補充量に応じ
てめっき液中の副生成物を活性炭濾過で除去する工程と
を含むことを特徴として構成される。
The method for managing a copper sulfate plating bath of the present invention includes a step of sampling a certain amount of plating solution from a copper sulfate plating bath, and quantifying the additive concentration in the sampled solution by a potential scanning stripping method using a rotating electrode. A process, a process of calculating the missing additive material from the additive concentration, a process of replenishing the missing additive, and a process of removing by-products in the plating solution by activated carbon filtration according to the cumulative replenishment amount of the additive. It is characterized by including a process.

本発明によれば硫B銅めっき浴の添加剤濃度を自動的に
測定し、添加剤を基準濃度迄補充すると共に添加剤の積
算補充量に応じ活性炭濾過を行う工程を有するのて、め
っき浴の安定性が保たれ、めっき仕上り不良を防止でき
る。また一定の硫酸銅めっき物性を維持てきる。
According to the present invention, the plating bath has a step of automatically measuring the additive concentration in the copper sulfur plating bath, replenishing the additive to the standard concentration, and performing activated carbon filtration according to the cumulative replenishment amount of the additive. The stability of the coating is maintained and defects in the plating finish can be prevented. In addition, certain physical properties of copper sulfate plating can be maintained.

〔実施例〕〔Example〕

次に、本発明について図面を参照して説明する。第1図
は本発明の一実施例の構成図である。
Next, the present invention will be explained with reference to the drawings. FIG. 1 is a block diagram of an embodiment of the present invention.

硫酸銅めっき槽1より、]時間毎に200m1を添加剤
自動分析装置2にサンプリンタする。添加剤自動分析装
置2にて分析した分析値をコントロ一ラー3にて演算し
添加剤濃度を標準値]○m1/Lに合わせる為の補充量
を定量ポンプ4に伝送する。又、コントローラー3によ
り添加剤の積算補充量を演算し補充量が20OLに達す
る毎に活性炭濾過循環ポンプ6に伝送し、5時間活性炭
濾過槽5にて濾過処理を行う。
From the copper sulfate plating tank 1, 200 ml is sampled every hour into the additive automatic analyzer 2. The analysis value analyzed by the automatic additive analyzer 2 is calculated by the controller 3, and the replenishment amount to adjust the additive concentration to the standard value]○ml/L is transmitted to the metering pump 4. Further, the controller 3 calculates the cumulative replenishment amount of the additive, and every time the replenishment amount reaches 20 OL, it is transmitted to the activated carbon filtration circulation pump 6, and filtration processing is performed in the activated carbon filtration tank 5 for 5 hours.

上述した方法により1時間毎の添加剤濃度の測定値に基
づく添加剤の補充及びその補充量200L毎の活性炭濾
過を繰り返しながら、硫酸銅めっき浴中の添加剤濃度の
管理を行う。
Using the method described above, the additive concentration in the copper sulfate plating bath is managed by repeating additive replenishment based on the additive concentration measurement value every hour and activated carbon filtration every 200 L of replenishment.

第2図は本発明の実施例2の構成図である。硫酸銅めっ
き槽7より、1時間毎に200m1を添加剤自動分析装
置8にサンプリングし分析した分析値をコントローラー
9にて演算し添加剤濃度を標準値10 m l / L
に合わせる為の補充1を定量ポンプ10に伝送する。又
、コントローラー9により添加剤の積算補充量を演算し
補充量が20OLに達する毎に活性炭濾過循環ポンプ1
に伝送し、5時間活性炭濾過フィルター14にて濾過処
理を行う。
FIG. 2 is a configuration diagram of a second embodiment of the present invention. From the copper sulfate plating tank 7, 200 ml is sampled every hour into the automatic additive analyzer 8, and the analyzed value is calculated by the controller 9, and the additive concentration is set to the standard value of 10 ml/L.
Replenishment 1 is transmitted to the metering pump 10 to match the amount. In addition, the controller 9 calculates the cumulative replenishment amount of the additive, and every time the replenishment amount reaches 20OL, the activated carbon filtration circulation pump 1 is activated.
and filtered through an activated carbon filter 14 for 5 hours.

上述した方法により1時間毎の添加剤濃度測定値の積算
印加電流値5000AHに基づく添加剤の補充及びその
補充量20OL毎の活性炭濾過を繰り返しながら、硫r
1i銅めっき浴中の添加剤濃度の管理を行う。この実施
例では添加剤補充を自動分析装置と積算電流値の併用に
より行う為、硫酸銅めっき浴中添加剤濃度のバラツキを
小さくすることかでき、また活性炭処理を濾過フィルタ
ーを用いて行う為、フロアスペースを濾過槽を使用する
場合よりも縮小化できるという利点かある。
Using the method described above, while repeating additive replenishment based on the cumulative applied current value of 5000 AH based on the additive concentration measurement value every hour and activated carbon filtration every 20 OL of the replenishment amount, sulfur r.
Control the concentration of additives in the 1i copper plating bath. In this example, since additive replenishment is performed using an automatic analyzer and integrated current value, it is possible to reduce the variation in additive concentration in the copper sulfate plating bath.Also, since the activated carbon treatment is performed using a filtration filter, This has the advantage that the floor space can be made smaller than when using a filtration tank.

〔発明の効果〕〔Effect of the invention〕

前述した様に本発明は、硫酸銀めっき浴の添加剤濃度を
自動的に測定し、添加剤を基準濃度まて補充すると共に
添加剤の積算補充量に応し活性炭濾過を行う工程を有す
るのて硫酸銀めっき浴の添加剤濃度を一定範囲に維持す
ることができ、下記の効果が得られる。
As mentioned above, the present invention has a step of automatically measuring the additive concentration in the silver sulfate plating bath, replenishing the additive to the standard concentration, and performing activated carbon filtration according to the cumulative replenishment amount of the additive. The additive concentration in the silver sulfate plating bath can be maintained within a certain range, and the following effects can be obtained.

(1)めっき浴の安定性が保たれ、めっき仕上り不良を
防止できる。
(1) Stability of the plating bath is maintained and poor plating finish can be prevented.

(2)一定の硫酸銅めっき物性か維持てきる。(2) Constant physical properties of copper sulfate plating can be maintained.

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

第1図は本発明の一実施例を構成を示すブロック図、第
2図は実施例2の構成を示すブロック図である。 1・・・硫酸銅めっき槽、2・・添加剤自動分析装置、
3・・コン)・ローラー、4・・・添加剤定量ポンプ、
4a・・添加剤タンク、5・・・活性炭濾過槽、6、活
性炭濾過槽循環ポンプ、7・・硫酸銅めっき槽、8・・
添加剤自動分析装置、9・・コントローラー、10・・
添加剤定量ポンプ、10a・・・添加剤タンク、11・
・・積算電流計、12・・・添加剤定期補充ポンプ、1
2a・・・添加剤定期補充タンク、13・・活性炭濾過
循環ポンプ、14・・・活性炭濾過フィルター。 代理人 弁理士  内 原  習 j≧S ノ’aX ンXCa 兜 1 囚
FIG. 1 is a block diagram showing the configuration of an embodiment of the present invention, and FIG. 2 is a block diagram showing the configuration of a second embodiment. 1... Copper sulfate plating tank, 2... Additive automatic analyzer,
3. Controller) roller, 4. Additive metering pump,
4a... Additive tank, 5... Activated carbon filtration tank, 6, Activated carbon filtration tank circulation pump, 7... Copper sulfate plating tank, 8...
Additive automatic analyzer, 9...controller, 10...
Additive metering pump, 10a...Additive tank, 11.
... Integral ammeter, 12 ... Additive regular replenishment pump, 1
2a... Additive regular replenishment tank, 13... Activated carbon filtration circulation pump, 14... Activated carbon filtration filter. Agent Patent Attorney Uchihara Xij≧S ノ'aX んXCa Kabuto 1 Prisoner

Claims (1)

【特許請求の範囲】[Claims] 硫酸銅めっき槽から一定量のめっき液をサンプリングす
る工程と、回転電極を用いた電位走査ストリッピング法
により前記サンプリング液中の添加剤濃度を定量する工
程と、その添加剤濃度から不足する添加材料を演算する
工程と、不足する添加剤を補充する工程と、添加剤の積
算補充量に応じてめっき浴中の副生成物を活性炭濾過で
除去する工程とを有することを特徴とする硫酸銅めっき
浴の管理方法。
A step of sampling a certain amount of plating solution from a copper sulfate plating tank, a step of quantifying the additive concentration in the sampled solution by a potential scanning stripping method using a rotating electrode, and determining the missing additive material from the additive concentration. Copper sulfate plating characterized by comprising a step of calculating, a step of replenishing missing additives, and a step of removing by-products in the plating bath by activated carbon filtration according to the cumulative replenishment amount of additives. How to manage your bath.
JP2315358A 1990-11-20 1990-11-20 Management method of copper sulfate plating bath Expired - Fee Related JP2558388B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2315358A JP2558388B2 (en) 1990-11-20 1990-11-20 Management method of copper sulfate plating bath

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2315358A JP2558388B2 (en) 1990-11-20 1990-11-20 Management method of copper sulfate plating bath

Publications (2)

Publication Number Publication Date
JPH04187800A true JPH04187800A (en) 1992-07-06
JP2558388B2 JP2558388B2 (en) 1996-11-27

Family

ID=18064456

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2315358A Expired - Fee Related JP2558388B2 (en) 1990-11-20 1990-11-20 Management method of copper sulfate plating bath

Country Status (1)

Country Link
JP (1) JP2558388B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016174705A1 (en) * 2015-04-27 2016-11-03 株式会社Jcu Method for managing copper sulfate plating solution

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016174705A1 (en) * 2015-04-27 2016-11-03 株式会社Jcu Method for managing copper sulfate plating solution
CN107532324A (en) * 2015-04-27 2018-01-02 株式会社杰希优 The management method of copper sulfate bath
JPWO2016174705A1 (en) * 2015-04-27 2018-02-15 株式会社Jcu Management method of copper sulfate plating solution

Also Published As

Publication number Publication date
JP2558388B2 (en) 1996-11-27

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