JPH0633249A - System for automatically controlling copper electroless-plating bath - Google Patents

System for automatically controlling copper electroless-plating bath

Info

Publication number
JPH0633249A
JPH0633249A JP19363392A JP19363392A JPH0633249A JP H0633249 A JPH0633249 A JP H0633249A JP 19363392 A JP19363392 A JP 19363392A JP 19363392 A JP19363392 A JP 19363392A JP H0633249 A JPH0633249 A JP H0633249A
Authority
JP
Japan
Prior art keywords
copper plating
solution
copper
plating solution
formaldehyde
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
JP19363392A
Other languages
Japanese (ja)
Other versions
JP3099531B2 (en
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 JP04193633A priority Critical patent/JP3099531B2/en
Publication of JPH0633249A publication Critical patent/JPH0633249A/en
Application granted granted Critical
Publication of JP3099531B2 publication Critical patent/JP3099531B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Chemically Coating (AREA)

Abstract

PURPOSE:To provide a system capable of automatically controlling a copper plating soln., especially its pH, with precision in the copper electroless-plating bath. CONSTITUTION:The copper concn., HCHO (reducing agent) concn. and pH of a copper plating soln. are controlled by adding solns. of CuSO4, HCHO and sodium hydroxide. In this case, since the pH of the soln. is lowered by addition of HCHO soln., the amt. of NaOH soln. to be added is determined in consideration of the amt. of the NaOH soln. necessary to adjust the pH, and the NaOH soln. is added.

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、銅めっき操作中の銅めっき
液各成分の管理、特に銅めっき液のpHを精度良く管理
す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, which can control each component of a copper plating solution during a copper plating operation, and particularly can accurately control the pH of the copper plating solution. The present invention relates to an electroless copper plating bath automatic management system.

【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、被めっき体が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 Compared with the electroplating method, the electroless plating method can obtain a coating of uniform thickness on all parts only by contacting the object to be plated with the plating solution, and the hardness of the deposits. There are features such as high price. For that purpose, it is necessary to appropriately manage the copper plating solution.

【0003】従来、無電解銅めっき浴の管理は、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
値より低い場合は、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操作を継続している。この
際、各成分を独立的に別々に管理するため、各成分が相
互に影響して理論添加量を添加しても管理値に調整され
ない場合が多い。
Conventionally, control of an electroless copper plating bath is an item necessary for control of a copper plating solution. For example, copper concentration, reducing agent concentration, and pH value are measured over time, and a preset control value is used. If it is low, the copper plating operation is continued while adding the replenisher to adjust the concentration of each component to the control value. At this time, since each component is controlled independently and independently, in many cases, each component influences each other, and even if the theoretical addition amount is added, the control value is not adjusted in many cases.

【0004】[0004]

【発明が解決しようとする課題】本発明は、無電解めっ
きの操作中に、銅めっき液の成分組成を予め設定した管
理値に調整するために各成分を補充添加するとき、銅め
っき液のpHを管理値に精度良く調整することができる
無電解銅めっき浴自動管理システムを提供することを目
的とする。
DISCLOSURE OF THE INVENTION The present invention provides a method for replenishing and adding each component during the electroless plating operation in order to adjust the component composition of the copper plating solution to a preset control value. An object of the present invention is to provide an electroless copper plating bath automatic control system capable of accurately adjusting pH to a control value.

【0005】[0005]

【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において、銅めっき操作中に
添加した各成分による銅めっき液のpHの変化を調整す
るに要するpH調整剤の添加量を複合的に演算して決定
することを特徴とする。
The electroless copper plating bath automatic management system according to the present invention is an electroless copper plating solution comprising a copper salt, a reducing agent and a pH adjusting agent, and each component added during the copper plating operation. It is characterized in that the addition amount of the pH adjusting agent required for adjusting the change in the pH of the copper plating solution due to the above is calculated by complex calculation.

【0006】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調節剤は水酸化
ナトリウム溶液である。
Preferably, the copper salt is a copper sulphate solution, the reducing agent is a formaldehyde solution and the pH adjusting agent is a sodium hydroxide solution.

【0007】[0007]

【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値であつて、銅めっき操作中は経時的
に銅めっき液中の各成分を測定する。その測定値に基づ
き、各成分濃度を管理値にまで調整するに要する各成分
の添加量を決定して、銅めっき液に補充添加することに
より、銅めっき液を調整する。
The control items of the copper plating solution are copper concentration, formaldehyde concentration and pH value, and each component in the copper plating solution is measured over time during the copper plating operation. Based on the measured values, the addition amount of each component required to adjust the concentration of each component to a control value is determined, and the copper plating liquid is adjusted by supplementing and adding to the copper plating liquid.

【0008】ホルムアルデヒド濃度の調整のため、ホル
ムアルデヒドを銅めっき液に添加すると、銅めっき液の
pHが低下する。この場合、銅めっき液の組成は管理値
に正確に調整されない。このような銅めっき液を使用し
た場合、被めっき製品の品質不良の原因となる。
When formaldehyde is added to the copper plating solution for adjusting the formaldehyde concentration, the pH of the copper plating solution is lowered. In this case, the composition of the copper plating solution is not accurately adjusted to the control value. When such a copper plating solution is used, it may cause poor quality of the product to be plated.

【0009】これに対し、ホルムアルデヒドの添加によ
る銅めっき液のpH低下を調整するに要する水酸化ナト
リウム添加量を加算して、水酸化ナトリウム添加量を決
定して銅めっき液に補充添加すると、銅めっき液組成を
精度良く管理値に調整することができる。このように適
確に管理された銅めっき液を使用することにより、良好
な品質の被めっき製品を得ることができる。
On the other hand, if the amount of sodium hydroxide added to adjust the pH drop of the copper plating solution due to the addition of formaldehyde is added to determine the amount of sodium hydroxide added and the copper plating solution is replenished and added, copper is added. The plating solution composition can be adjusted to a control value with high accuracy. By using the copper plating solution properly managed in this way, it is possible to obtain a product to be plated of good quality.

【0010】[0010]

【実施例】以下、実施例において、本発明を詳しく説明
する。
EXAMPLES The present invention will be described in detail below with reference to examples.

【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)20ml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pH12.4
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2.5g/l、
ホルムアルデヒド2.5ml/lであつた。
Example 100 g of copper sulfate (pentahydrate), formaldehyde (37
% Water solution) in 10 liters of water and pH 12.4 with 1 mol / l sodium hydroxide solution.
Then, 10 liters of the copper plating solution was prepared and used. The concentration of each component in this copper plating solution is 2.5 g / l of copper,
Formaldehyde was 2.5 ml / l.

【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。銅めっき処理
2時間後、銅めっき液の各成分の濃度は、銅2.2g/
l、ホルムアルデヒド0.8ml/lに変化し、pHは
12.2にまで低下した。この銅めっき液組成の調整
を、63g/l硫酸銅溶液(A液)、37%ホルムアル
デヒド溶液(B液)、1mol/l水酸化ナトリウム溶
液(C液)を使用して行つた。
The copper plating reaction was carried out at 70 ° C., and an epoxy copper clad laminate was used as a sample to be plated. Two hours after the copper plating treatment, the concentration of each component of the copper plating solution was 2.2 g of copper /
1 and formaldehyde changed to 0.8 ml / l, and the pH dropped to 12.2. The composition of the copper plating solution was adjusted using 63 g / l copper sulfate solution (solution A), 37% formaldehyde solution (solution B), and 1 mol / l sodium hydroxide solution (solution C).

【0013】銅濃度の調整は、図2から調整に必要なA
液(硫酸銅溶液)の添加量31.7mlを求め、銅めっ
き液に添加して行つた。ホルムアルデヒド濃度の調整
は、図3から調整に必要なB液(ホルムアルデヒド溶
液)の添加量25mlを求め、銅めっき液に添加して行
つた。pHの調整は、先ず図1から銅めっき液のpHを
調整するに必要なC液(水酸化ナトリウム溶液)の添加
量50ml(T)を求めた。次いで、B液(ホルムアル
デヒド溶液)を銅めっき液に添加したことによる銅めっ
き液のpH低下を図4から求め、図1からこのpH低下
を調整するに必要な水酸化ナトリウム溶液の添加量25
ml(S)を求めた。このTとSを合せた水酸化ナトリ
ウム溶液添加量75mlを銅めっき液に添加して、銅め
っき液のpH調整を行つた。
The adjustment of the copper concentration is performed according to FIG.
The addition amount of the solution (copper sulfate solution) of 31.7 ml was determined and added to the copper plating solution. The formaldehyde concentration was adjusted by obtaining 25 ml of the solution B (formaldehyde solution) required for the adjustment from FIG. 3 and adding it to the copper plating solution. To adjust the pH, first, from FIG. 1, an addition amount of 50 ml (T) of the solution C (sodium hydroxide solution) necessary for adjusting the pH of the copper plating solution was obtained. Next, the pH drop of the copper plating solution due to the addition of solution B (formaldehyde solution) to the copper plating solution was obtained from FIG. 4, and the addition amount of the sodium hydroxide solution necessary to adjust this pH drop was calculated from FIG.
ml (S) was determined. A total of 75 ml of the sodium hydroxide solution added with T and S was added to the copper plating solution to adjust the pH of the copper plating solution.

【0014】その結果、得られた銅めっき液のpHは1
2.4であつて、銅めっき液の調整は適正に行うことが
できた。このような銅めっき液を使用することにより、
良好な銅めっき製品を得ることができた。
As a result, the pH of the obtained copper plating solution is 1
In 2.4, the copper plating solution could be adjusted properly. By using such a copper plating solution,
A good copper-plated product could be obtained.

【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)20ml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pH12.4
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2.5g/l、
ホルムアルデヒド2.5ml/lであつた。
Comparative Example 100 g of copper sulfate (pentahydrate), formaldehyde (37
% Water solution) in 10 liters of water and pH 12.4 with 1 mol / l sodium hydroxide solution.
Then, 10 liters of the copper plating solution was prepared and used. The concentration of each component in this copper plating solution is 2.5 g / l of copper,
Formaldehyde was 2.5 ml / l.

【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。銅めっき処理
2時間後、銅めっき液の各成分の濃度は、銅2.2g/
l、ホルムアルデヒド0.8ml/lに変化し、pHは
12.2にまで低下した。この銅めっき液組成の調整
を、63g/l硫酸銅溶液(A液)、37%ホルムアル
デヒド溶液(B液),1mol/l水酸化ナトリウム溶
液(C液)を使用して行つた。
The copper plating reaction was carried out at 70 ° C., and an epoxy copper clad laminate was used as a sample to be plated. Two hours after the copper plating treatment, the concentration of each component of the copper plating solution was 2.2 g of copper /
1 and formaldehyde changed to 0.8 ml / l, and the pH dropped to 12.2. The composition of the copper plating solution was adjusted using 63 g / l copper sulfate solution (solution A), 37% formaldehyde solution (solution B), and 1 mol / l sodium hydroxide solution (solution C).

【0017】銅濃度の調整は、図2から必要なA液(硫
酸銅溶液)の添加量31.7mlを求め、銅めっき液に
添加して行つた。ホルムアルデヒド濃度の調整は、図3
から必要なB液(ホルムアルデヒド溶液)の添加量25
mlを求め、銅めっき液に添加して行つた。pHの調整
は、図1から必要なB液(硫酸銅溶液)の添加量50m
lを求め、銅めっき液に添加して行つた。
The copper concentration was adjusted by determining the required addition amount of solution A (copper sulfate solution) of 31.7 ml from FIG. 2 and adding it to the copper plating solution. Figure 3 shows the adjustment of formaldehyde concentration.
Amount of liquid B (formaldehyde solution) required from 25
ml was determined and added to the copper plating solution. To adjust the pH, add the required amount of solution B (copper sulfate solution) of 50 m from Fig. 1.
1 was determined and added to the copper plating solution.

【0018】その結果、得られた銅めっき液のpHは1
2.3にとどまり、銅めっき液の調整は適正に行うこと
ができなかつた。このような銅めっき液を使用すると良
好なめっき製品を得ることができなかつた。
As a result, the pH of the obtained copper plating solution was 1
Only 2.3, and the copper plating solution could not be properly adjusted. It was not possible to obtain a good plated product by using such a copper plating solution.

【0019】[0019]

【発明の効果】無電解銅めっき操作中、銅めっき液の管
理項目である銅濃度、ホルムアルデヒド濃度、pHを調
整するために、硫酸銅溶液、ホルムアルデヒド溶液、水
酸化ナトリウム溶液を添加する。この場合、ホルムアル
デヒド溶液を添加すると銅めっき液のpHが低下する。
このpH低下を調整するに要する水酸化ナトリウム溶液
も加算して、水酸化ナトリウム溶液添加量を決定し銅め
っき液に添加することにより、銅めっき液のpHは精度
良く管理値に調整される。このように適確に管理された
銅めっき液を使用することにより、良好な品質の被めっ
き製品を得ることができる。
During the electroless copper plating operation, a copper sulfate solution, a formaldehyde solution, and a sodium hydroxide solution are added in order to adjust the copper concentration, formaldehyde concentration, and pH, which are control items of the copper plating solution. In this case, addition of the formaldehyde solution lowers the pH of the copper plating solution.
The pH of the copper plating solution is accurately adjusted to a control value by adding the sodium hydroxide solution required for adjusting this pH decrease, determining the addition amount of the sodium hydroxide solution, and adding it to the copper plating solution. By using the copper plating solution properly managed in this way, it is possible to obtain a product to be plated of good quality.

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

【図1】水酸化ナトリウム溶液の添加による銅めっき液
のpH変化を示したグラフである。
FIG. 1 is a graph showing a change in pH of a copper plating solution due to addition of a sodium hydroxide solution.

【図2】硫酸銅溶液の添加による銅めっき液中の銅濃度
の変化を示したグラフである。
FIG. 2 is a graph showing changes in copper concentration in a copper plating solution due to addition of a copper sulfate solution.

【図3】ホルムアルデヒド溶液の添加による銅めっき液
中のホルムアルデヒド濃度の変化を示したグラフであ
る。
FIG. 3 is a graph showing changes in formaldehyde concentration in a copper plating solution due to addition of a formaldehyde solution.

【図4】ホルムアルデヒド溶液の添加による銅めっき液
のpH変化を示したグラフである。
FIG. 4 is a graph showing a pH change of a copper plating solution due to addition of a formaldehyde solution.

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
解銅めっき液において、銅めっき操作中に補充添加した
各成分による銅めっき液のpHの変化を調整するに要す
るpH調整剤の添加量を複合的に演算して決定すること
を特徴とする無電解銅めっき浴自動管理システム。
1. An electroless copper plating solution comprising a copper salt, a reducing agent and a pH adjusting agent, which is a pH adjusting agent necessary for adjusting the change in pH of the copper plating solution due to each component replenished and added during the copper plating operation. An electroless copper plating bath automatic management system characterized in that the additive amount is compositely calculated and determined.
【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調節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 adjusting agent is sodium hydroxide.
JP04193633A 1992-07-21 1992-07-21 Electroless copper plating bath automatic management system Expired - Fee Related JP3099531B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04193633A JP3099531B2 (en) 1992-07-21 1992-07-21 Electroless copper plating bath automatic management system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04193633A JP3099531B2 (en) 1992-07-21 1992-07-21 Electroless copper plating bath automatic management system

Publications (2)

Publication Number Publication Date
JPH0633249A true JPH0633249A (en) 1994-02-08
JP3099531B2 JP3099531B2 (en) 2000-10-16

Family

ID=16311192

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04193633A Expired - Fee Related JP3099531B2 (en) 1992-07-21 1992-07-21 Electroless copper plating bath automatic management system

Country Status (1)

Country Link
JP (1) JP3099531B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011506769A (en) * 2007-12-12 2011-03-03 ラム リサーチ コーポレーション Method and apparatus for analysis and control of plating solutions

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011506769A (en) * 2007-12-12 2011-03-03 ラム リサーチ コーポレーション Method and apparatus for analysis and control of plating solutions
US9128493B2 (en) 2007-12-12 2015-09-08 Lam Research Corporation Method and apparatus for plating solution analysis and control

Also Published As

Publication number Publication date
JP3099531B2 (en) 2000-10-16

Similar Documents

Publication Publication Date Title
US5248527A (en) Process for electroless plating tin, lead or tin-lead alloy
JP4091518B2 (en) Electroless deposition of metals
US5269838A (en) Electroless plating solution and plating method with it
US5614003A (en) Method for producing electroless polyalloys
US4600609A (en) Method and composition for electroless nickel deposition
US4406250A (en) Apparatus for controlling electroless plating bath
US3033703A (en) Electroless plating of copper
US4152164A (en) Electroless nickel plating
US3032436A (en) Method and composition for plating by chemical reduction
US4242180A (en) Ammonia free palladium electroplating bath using aminoacetic acid
US3264199A (en) Electroless plating of metals
US4325990A (en) Electroless copper deposition solutions with hypophosphite reducing agent
US4913787A (en) Gold plating bath and method
US4724188A (en) Magnetic recording medium
JP2000503354A (en) Removal of orthophosphite ions from electroless nickel plating bath
US6524642B1 (en) Electroless metal-plating process
EP0319755B1 (en) Method for controlling plating on seeded surfaces
US3468676A (en) Electroless gold plating
JPH0633249A (en) System for automatically controlling copper electroless-plating bath
IT9067773A1 (en) METHOD FOR PREPARING ALUMINUM MEMORY DISCS WITH A SMOOTH PLATED FINISH
JPH0565661A (en) Manufacturing method of electroless nickel plating film
US2827398A (en) Electroless iron plating
US5200047A (en) Plating solution automatic control
US3667972A (en) Chemical nickel plating baths
CA1062649A (en) Electrodeposition of tin-containing alloys and bath therefor

Legal Events

Date Code Title Description
S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080818

Year of fee payment: 8

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080818

Year of fee payment: 8

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090818

Year of fee payment: 9

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 10

Free format text: PAYMENT UNTIL: 20100818

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100818

Year of fee payment: 10

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 11

Free format text: PAYMENT UNTIL: 20110818

LAPS Cancellation because of no payment of annual fees