JPS6032820B2 - Method and device for controlling reducing agent concentration in chemical copper plating solution - Google Patents

Method and device for controlling reducing agent concentration in chemical copper plating solution

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Publication number
JPS6032820B2
JPS6032820B2 JP52064813A JP6481377A JPS6032820B2 JP S6032820 B2 JPS6032820 B2 JP S6032820B2 JP 52064813 A JP52064813 A JP 52064813A JP 6481377 A JP6481377 A JP 6481377A JP S6032820 B2 JPS6032820 B2 JP S6032820B2
Authority
JP
Japan
Prior art keywords
potential
plating solution
formaldehyde
copper plating
detected
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
Application number
JP52064813A
Other languages
Japanese (ja)
Other versions
JPS541093A (en
Inventor
齊 岡
信夫 佐藤
健二 中村
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP52064813A priority Critical patent/JPS6032820B2/en
Publication of JPS541093A publication Critical patent/JPS541093A/en
Publication of JPS6032820B2 publication Critical patent/JPS6032820B2/en
Expired legal-status Critical Current

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  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
  • Chemically Coating (AREA)
  • Control Of Non-Electrical Variables (AREA)

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は、化学銅めつき液中の還元剤濃度の制御方法と
制御装置に係り、特に化学鋼めつき液中のホルムアルデ
ヒド濃度の制御方法と制御装置に関する。
[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a method and device for controlling the concentration of a reducing agent in a chemical copper plating solution, and particularly to a method and a control device for controlling the concentration of formaldehyde in a chemical steel plating solution. Regarding a control device.

〔発明の背景〕[Background of the invention]

最近、絶縁基板の所望部分に、直接化学鋼めつきを5〜
3餌時間行って配線パターンを形成し、プリント配線板
を製造することが行われている。
Recently, chemical steel plating has been applied directly to desired parts of insulating substrates.
Printed wiring boards are manufactured by forming wiring patterns for three hours.

そして、上記配線パターンは、導体としての電気特性は
言うに及ばず機械特性がすぐれている事が必要である。
しかし、上記配線パターンの特性は、化学鋼めつき液の
組成、なかでも還元剤であるホルムアルデヒドの濃度に
左右される。即ち、ホルムアルデヒドはめつき時の反応
、自己分解、蒸発などで急激に消費される。そして、ホ
ルムアルデヒド濃度が所望の値より小さくなるとめつき
速度がおそくなり、所望の値より大きくなるとめつき皮
膜がもろくなり、かつめつき液が分解してしまう不都合
があった。このため、化学鋼めつき液中のホルムアルデ
ヒド濃度を長時間所望の値に保つ必要がある。
The wiring pattern needs to have excellent mechanical properties as well as electrical properties as a conductor.
However, the characteristics of the above wiring pattern depend on the composition of the chemical steel plating solution, especially the concentration of formaldehyde, which is a reducing agent. That is, formaldehyde is rapidly consumed by reactions during plating, self-decomposition, evaporation, etc. When the formaldehyde concentration is lower than a desired value, the plating speed becomes slow, and when the formaldehyde concentration is higher than the desired value, the plating film becomes brittle and the plating solution decomposes. Therefore, it is necessary to maintain the formaldehyde concentration in the chemical steel plating solution at a desired value for a long time.

そのためには、長時間にわたってホルムアルデヒド濃度
を精度良く測定することが要求される。従来、化学鋼め
つき液中のホルムアルデヒド濃度は、採取した一定量の
めつき液を酸で中和し、その後亜硫酸ソーダを混合し、
下記‘1ー式のようにホルムアルデヒドと亜硫酸ソーダ
とを反応させ、この際生成した苛性ソーダ量をガラス電
極と参照電極により掛値として測定し、このpH値が一
定値になるようにホルムアルデヒド濃度を調節していた
For this purpose, it is required to accurately measure formaldehyde concentration over a long period of time. Conventionally, the formaldehyde concentration in chemical steel plating solutions was determined by neutralizing a certain amount of the plating solution with acid, then mixing it with sodium sulfite,
Formaldehyde and sodium sulfite are reacted as shown in formula 1 below, and the amount of caustic soda produced at this time is measured as a multiplication value using a glass electrode and a reference electrode, and the formaldehyde concentration is adjusted so that this pH value becomes a constant value. Was.

HCHO+Na2S03十日20エNaOH+C比(N
aS03)OH ・・・・・・【1’しか
し、上記の方法は、被測定液の柵が13〜14になるた
め、ガラス電極はアルカリで侵されて劣化し、かつ塩誤
、差も生じるため、時間がたっと正確なM値が測定でき
なくなり、長時間にわたって正確なホルムアルデヒド濃
度管理ができなかった。
HCHO+Na2S03 10 days 20 days NaOH+C ratio (N
aS03) OH ...... [1' However, in the above method, since the fence of the liquid to be measured is 13 to 14, the glass electrode is attacked by alkali and deteriorates, and salt errors and differences also occur. Therefore, it became impossible to accurately measure the M value over time, and accurate formaldehyde concentration control could not be performed over a long period of time.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、上託した従来技術の欠点をなくし、長
時間にわたって精度良く化学鋼めつき液中の還元剤濃度
を制御する方法とその装置を提供するにある。
SUMMARY OF THE INVENTION An object of the present invention is to eliminate the drawbacks of the prior art and provide a method and apparatus for controlling the reducing agent concentration in a chemical steel plating solution with high accuracy over a long period of time.

〔発明の概要〕[Summary of the invention]

そして、上記目的は鋼イオンと、鋼イオンの鏡化剤と、
ホルムアルデヒドと、アルカリ金属の水酸化物と、水と
からなる化学鋼めつき液の一定容量にホルムアルデヒド
配合量より過剰の亜硫酸ナトリウムと、母6〜12でp
H緩衝効果を示すpH緩衝剤を一定量加え、亜硫酸ナト
リウム、化学鋼めつき液中のホルムアルデヒドとを迅速
、かつ不純物の影響もなく前記‘1’式のように反応さ
せ、ついでヨウ素と、斑2〜9でpH緩衝効果を示すp
H緩衝剤を一定量加えて、化学鋼めつき液中に残存する
亜硫酸ナトリウムとヨウ素とを■式のように反応させる
And, the above purpose is to use steel ions, a mirroring agent for steel ions,
Add sodium sulfite in excess of the amount of formaldehyde to a certain volume of a chemical steel plating solution consisting of formaldehyde, alkali metal hydroxide, and water, and add p.p.
A certain amount of a pH buffering agent exhibiting H buffering effect is added, and sodium sulfite and formaldehyde in a chemical steel plating solution are reacted quickly and without the influence of impurities as in the formula '1' above. p which shows pH buffering effect between 2 and 9
By adding a certain amount of H buffer, the sodium sulfite and iodine remaining in the chemical steel plating solution are allowed to react as shown in equation (2).

Na2S03十12十&0こNa2S04十2HI
…・・・■この際ホルムアルデヒドが所定値より過剰
で、ヨウ素が残存するときは、ヨウ素は以下{3’式の
ような平衝状態になる。
Na2S03 1120&0koNa2S0412HI
...■ At this time, if formaldehyde is in excess of a predetermined value and iodine remains, iodine will be in an equilibrium state as shown in equation {3' below.

12十をこ21‐ …・
・・{3}一方、ホルムアルデヒドが所定値より不足し
、亜硫酸ナトリウムが残存するときは、化学鋼めつき液
の自然電位を示す。
120 ko21-...
...{3} On the other hand, when formaldehyde is insufficient than the predetermined value and sodium sulfite remains, it indicates the natural potential of the chemical steel plating solution.

すなわち、この‘31式の平衡反応で生ずる平衝電位か
めつき液の自然電位かを検出して化学鋼めつき液中のホ
ルムアルデヒド濃度を測定する。
That is, the formaldehyde concentration in the chemical steel plating solution is measured by detecting the natural potential of the equilibrium potential of the plating solution generated by this '31 equation equilibrium reaction.

すなわち、検出された電位と設定電位とを比較してホル
ムアルデヒド濃度を制御する。なお、pHが2より小さ
いとヨウ素が分解してしまうので、上記‘3’の平衝反
応が起こらない。
That is, the formaldehyde concentration is controlled by comparing the detected potential and a set potential. Note that if the pH is less than 2, iodine will be decomposed, so the equilibrium reaction of '3' above will not occur.

また、靴が9より大きいと、{41式に示すようにヨウ
素が苛性ソーダと反応し、Nal○となり、12+2N
aOH十NaloェNal+日20 ……‘41
Nal0で亜硫酸が酸化されてしまい、めつき液の自然
亀位から、前記【31式の平衡肉位への電位変化が検出
できない。なお、電位は金又は白金を主亀極とし、これ
と参照電極を組み合わせて検出する。
Also, if the shoes are larger than 9, iodine reacts with caustic soda as shown in formula {41, becomes Nal○, and becomes 12+2N
aOH 10 Nalo 20...'41
Sulfite is oxidized by Nal0, and the change in potential from the natural level of the plating solution to the equilibrium level of formula 31 cannot be detected. Note that the potential is detected by using gold or platinum as a main electrode in combination with a reference electrode.

前記の柵6〜12で緩衝効果を有するpH緩衝剤は、リ
ン酸二水素カリウム、リン酸水素二ナトリウム、炭酸ナ
トリウム、ホウ砂、クエン酸ナトリウム、塩化アンモニ
ウム又はジメチルグリシムナトリウムが好ましい。
The pH buffering agent having a buffering effect in the fences 6 to 12 is preferably potassium dihydrogen phosphate, disodium hydrogen phosphate, sodium carbonate, borax, sodium citrate, ammonium chloride or sodium dimethylglycine.

また、前記のpH2〜9で緩衝効果を有するpH緩衝剤
は、クエン酸水素カリウム、リン酸二水素カリウム、ク
エン酸ナトリウム、グリシン又はフタル酸水素カリウム
が好ましい。
The pH buffer having a buffering effect at pH 2 to 9 is preferably potassium hydrogen citrate, potassium dihydrogen phosphate, sodium citrate, glycine, or potassium hydrogen phthalate.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明を実施例によって詳細に説明する。 Hereinafter, the present invention will be explained in detail with reference to Examples.

実施例 1 化学鋼めつき液組成 CuS04・QLO …・・・12タE
DTA−2Na ・・・・・・40タ
NaOH ・・・・・・11夕
日CHO ……3夕添加剤
・…・・少量水 ・・・・
・・全体を1〆とする量0 亜硫酸ナトリウム溶液組成
Na2S03 ・・・・・・1
8.9タNa2B40?・10日20 ・
・・・・・20タ水 ・・・・・・全体を1夕
とする量m ヨウ素溶液組成K1
・・…・40夕12
……12‐692タKH2P04
・・・・・・100タ水 ・・・・・・全体を
1夕とする量上記1の組成の化学鋼めつき液を図のめつ
き槽1から多連チューブポンプ2で毎時20泌の流速で
サンプリングし、同時に上記0の組成の亜硫酸ナトリウ
ム溶液を図の亜硫酸ナトリウム溶液槽から多連チューブ
ポンプ2で毎時20の‘の流速でサンプリングしT字管
5で混合した。
Example 1 Chemical steel plating liquid composition CuS04・QLO...12taE
DTA-2Na...40TaNaOH...11Yuhi CHO...3Yu Additive
・・・・・・A small amount of water ・・・・・・
・・・Amount to make the whole 1〆 0 Sodium sulfite solution composition Na2S03 ・・・・・・1
8.9 Ta Na2B40?・10th 20th ・
・・・・・・20 t water ・・・・Amount m to make the whole thing overnight Iodine solution composition K1
・・・・・・40 pm 12
...12-692ta KH2P04
・・・・・・100 tons of water ・・・Total amount for one night A chemical steel plating solution having the composition shown in 1 above is pumped from the plating tank 1 shown in the figure at a rate of 20 discharges per hour using the multiple tube pump 2. At the same time, a sodium sulfite solution having a composition of 0 was sampled from the sodium sulfite solution tank shown in the figure at a flow rate of 20' per hour using a multiple tube pump 2 and mixed in a T-tube 5.

さらに前記mの組成のヨウ素溶液をヨウ素溶液槽4から
多蓮チューブポンプで毎時20の‘の流速でサンプリン
グし、T字管6で上記の亜硫酸ナトljゥムを加えた化
学鋼めつき液に混合した。
Furthermore, the iodine solution having the composition m is sampled from the iodine solution tank 4 using a polyurethane tube pump at a flow rate of 20 minutes per hour, and is added to the chemical steel plating solution to which sodium sulfite has been added using the T-tube 6. Mixed.

なお、亜硫酸ナトリウム溶液とヨウ素溶液の添加童は以
下のようである。
The addition conditions for sodium sulfite solution and iodine solution are as follows.

先ず亜硫酸ナトリウムとホルムアルデヒドとの反応モル
比は、前認11式から1:1であることがわかる。また
亜硫酸ナトリウムとヨウ素との反応モル比も、前記【2
’式から1:1であることがわかる。次にめつき糟1中
の化学縮めつき液1中のホルムアルデヒド濃度をHmo
l/ク亜硫酸ナトリウム溶液槽3中の亜硫酸ナトリウム
溶液0中の亜硫酸ナトリウム濃度をSmol/そ、ヨウ
素溶液槽4中のヨウ素溶液m中のヨウ素濃度をYmol
/そとし、化学鋼めつき液1、亜硫酸ナトリウム溶液0
、ヨウ素溶液mの多連チューブポンプ2でのサンプリン
グ速度を夫々Vの【/hとすると、YXV=SXV一日
XV ・・…・【51則ち、■式
の関係が成立する。
First, it can be seen from the previous equation 11 that the reaction molar ratio between sodium sulfite and formaldehyde is 1:1. In addition, the reaction molar ratio between sodium sulfite and iodine is also the same as [2] above.
It can be seen from the formula that the ratio is 1:1. Next, the formaldehyde concentration in the chemical shrinkage solution 1 in the plating pot 1 is determined as Hmo
l/k Sodium sulfite concentration in sodium sulfite solution 0 in sodium sulfite solution tank 3 is Smol/so, iodine concentration in iodine solution m in iodine solution tank 4 is Ymol
/ Sotoshi, chemical steel plating solution 1, sodium sulfite solution 0
, the sampling rate of the iodine solution m in the multiple tube pump 2 is V/h, then YXV=SXV/day XV...[51 Therefore, the relationship of equation (2) holds true.

Y=S−日 ……{6’した
がって、H=0.1mol/そ(3夕/Z)、S=0.
19hol/〆(18.9夕/そ)とすれば、Y=0.
08hol/そ(12.692夕/そ)となる。
Y=S-day...{6' Therefore, H=0.1 mol/so(3 evening/Z), S=0.
If 19 hol/end (18.9 evening/so), then Y=0.
08 hol/so (12.692 evening/so).

この混合溶液は図の電位検出セル7に入り、白金電極8
と参照電極9との間で電位を検出しこの検出電位がデジ
タルボルトメータとデジタルコンパレータよりなる制御
装置のデジタルボルトメータに入力され検出電位が表示
され、この検出電位がデジタルコンパレータの設定電位
一0.1V(ホルムアルデヒド濃度、3.0夕/そに相
当)と比較されてホルムアルデヒド濃度の調節が開始さ
れた。化学鋼めつき液中のホルムアルデヒド濃度が3.
0夕/ぐより不足している時は、検出電位は表のM.1
〜M.5に示すように設定電位の−0.1Vより小さい
負の化学鋼めつき液の自然電位を示し、これらの場合は
検出電位と設定電位の差が信号となって電磁弁11が開
いてホルムアルデヒド補給槽12からホルムアルデヒド
溶液がめつさ槽1に補給され、検出電位が−0.1Vに
なったら補給を停止した。± ホルムアルデヒド濃度と
検出電位の関係また、化学鋼めつき液中のホルムアルデ
ヒド濃度が3.0夕/そより多いときは、検出電位は表
のM.6〜M.10に示すように設定電位の−0.1V
より大きい正の電位(前記【3}式の平衝電位)を示し
、これらの場合は検出電位と検出電位の差が信号となっ
てこの両者の値が等しくなる迄化学鋼めつき液にホルム
アルデヒド溶液が補給されなかった。
This mixed solution enters the potential detection cell 7 in the figure, and the platinum electrode 8
The detected potential is inputted to the digital voltmeter of the control device consisting of a digital voltmeter and a digital comparator, and the detected potential is displayed. .1 V (formaldehyde concentration, equivalent to 3.0 m/s), and the formaldehyde concentration began to be adjusted. The formaldehyde concentration in the chemical steel plating solution is 3.
When the detection potential is less than 0/g, the detection potential is M. in the table. 1
~M. 5 shows the natural potential of the chemical steel plating solution which is smaller than the set potential of -0.1V, and in these cases, the difference between the detected potential and the set potential serves as a signal to open the solenoid valve 11 and release formaldehyde. Formaldehyde solution was replenished from the supply tank 12 to the Metsusa tank 1, and when the detection potential reached -0.1V, the supply was stopped. ±Relationship between formaldehyde concentration and detection potential Also, when the formaldehyde concentration in the chemical steel plating solution is 3.0 μm or more, the detection potential is as shown in the table M. 6~M. -0.1V of the set potential as shown in 10.
In these cases, the difference between the detected potential and the detected potential becomes a signal, and formaldehyde is added to the chemical steel plating solution until the two values become equal. Solution was not replenished.

なお、電位検出セル7を出た亜硫酸ナトリウムとヨウ素
を加えた化学鋼めつき液は排出槽13へ廃出した。〔発
明の効果〕 すなわち、前記1の化学鋼めつき液に前記ロ,mの亜硫
酸ソーダ溶液、ヨウ素溶液を一定量混合し、この混合溶
液の電位を検出し、この検出電位が設定電位の−0.1
Vより小さい場合はホルムアルデヒドが補給され、大き
い場合はホルムアルデヒドの補給が停止され、ホルムア
ルデヒドの濃度制御を連続5餌時間行なったところ、士
5%の精度でホルムアルデヒド濃度が制御された。
Incidentally, the chemical steel plating solution containing sodium sulfite and iodine that came out of the potential detection cell 7 was discharged to a discharge tank 13. [Effects of the Invention] That is, a certain amount of the sodium sulfite solution and iodine solution of B and M are mixed with the chemical steel plating solution of 1 above, the potential of this mixed solution is detected, and this detected potential is - of the set potential. 0.1
If it was smaller than V, formaldehyde was replenished, and if it was larger, formaldehyde was stopped. When the formaldehyde concentration was controlled for 5 consecutive feeding periods, the formaldehyde concentration was controlled with an accuracy of -5%.

また、電極はアルカリで劣化せず、塩誤差も生じないの
で、さらに長時間精度良くホルムアルデヒド濃度が制御
できる。
Furthermore, since the electrodes are not degraded by alkali and salt errors do not occur, the formaldehyde concentration can be controlled with high precision for a longer period of time.

また、本発明の制御方法と制御装贋は、ホルムアルデヒ
ドを還元剤として用いる化学銀めつきの還元剤濃度の制
御にも適用できる。
Furthermore, the control method and control device of the present invention can also be applied to control of reducing agent concentration in chemical silver plating using formaldehyde as a reducing agent.

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

図はイb学鋼めつき液中のホルムアルデヒドの自動濃度
制御装置の構成図である。 1・・・・・・めつき糟、2・・・・・・多連チューブ
ポンプ、3・・・・・・亜硫酸ナトリウム溶液槽、4・
…・・ヨウ素溶液槽、7・・・…電位検出セル、8・・
・・・・白金電極、9・・・・・・参照電極、12・・
・・・・補給槽。
The figure is a block diagram of an automatic concentration control device for formaldehyde in a steel plating solution. 1...Metting pot, 2...Multiple tube pump, 3...Sodium sulfite solution tank, 4...
...Iodine solution tank, 7...Potential detection cell, 8...
...Platinum electrode, 9...Reference electrode, 12...
...Replenishment tank.

Claims (1)

【特許請求の範囲】 1 銅イオンと、銅イオンの錯化剤と、ホルムアルデヒ
ドと、アルカリ金属の水酸化物と、水とからなる化学銅
めつき液の一定容量に、前記ホルムアルデヒドの配合量
より過剰な亜硫酸ソーダと、pH6〜12でpH緩衝効
果を示すpH緩衝剤を加えて前記ホルムアルデヒドと前
記亜硫酸ソーダとを反応させ、ついで、これにヨウ素と
、pH2〜9でpH緩衝効果を有するpH緩衝剤を加え
て、残存する亜硫酸ソーダとヨウ素とを反応させて、ホ
ルムアルデヒド配合量が所望の値より少なく亜硫酸ナト
リウムが残存する場合は、制御装置の設定電位より小さ
い値の化学銅めつき液の自然電位を金又は白金の主電極
と参照電極により検出し、この検出電位と設定電位との
差が信号となつて、検出電位が設定電位と等しくなる迄
ホルムアルデヒドを化学めつき液に補給し、ホルムアル
デヒド配合量が所望の値より大きくヨウ素が残存する場
合は、制御装置の設定電位より大きい値のヨウ素分子I
_2とヨウ素イオンI^−の平衡電位を金又は白金の電
極と参照電極により検出し、この検出電位と設定電位の
差が信号となつて検出電位が設定電位と等しくなる迄ホ
ルムアルデヒドが化学銅めつき液に補給しないことを特
徴とする化学銅めつき液中の還元剤濃度の制御方法。 2 pH6〜12でpH緩衝効果を示すpH緩衝剤が、
リン酸二水素カリウム、リン酸水素二ナトリウム、炭酸
ナトリウム、ホウ砂、クエン酸ナトリウム、塩化アンモ
ニウムもしくはジメチルグリシムナトリウムであること
を特徴とする特許請求の範囲第1項記載の化学銅めつき
液中の還元剤濃度の制御方法。 3 pH2〜9でpH緩衝効果を有するpH緩衝剤が、
クエン酸水素カリウム、リン酸二水素カリウム、クエン
酸ナトリウム、グリシンもしくはフタル酸水素カリウム
であることを特徴とする特許請求の範囲第1項記載の化
学銅めつき液中の還元剤濃度の制御方法。 4 化学銅めつき液に、亜硫酸イオンとpH6〜12で
pH緩衝効果を有するpH緩衝剤を含む容液を一定容量
混合する装置と、ヨウ素とpH2〜9域で緩衝するpH
緩衝剤とを含む水容液を一定容量混合する装置と、この
混合液の電位を検出する装置と、検出した電位があらか
じめ設定した電位より小さい場合は、その電位差が信号
となつて検出電位と設定電位が等しくなるまでホルムア
ルデヒドを補給し、検出した電位があらかじめ設定した
電位より大きい場合は、その差が信号となつて、検出電
位が設定電位に等しくなる迄ホルムアルデヒドの補給を
停止する制御装置よりなることを特徴とする化学銅めつ
き液中の還元剤濃度制御装置。
[Claims] 1. A chemical copper plating solution consisting of copper ions, a complexing agent for copper ions, formaldehyde, an alkali metal hydroxide, and water is added to a certain volume of a chemical copper plating solution containing more than the amount of formaldehyde. The formaldehyde and the sodium sulfite are reacted by adding excess sodium sulfite and a pH buffering agent having a pH buffering effect at pH 6 to 12, and then iodine is added to this and a pH buffering agent having a pH buffering effect at pH 2 to 9. If the formaldehyde content is less than the desired value and sodium sulfite remains, use the natural chemical copper plating solution with a value lower than the set potential of the control device. The potential is detected by a gold or platinum main electrode and a reference electrode, and the difference between the detected potential and the set potential becomes a signal.Formaldehyde is replenished into the chemical plating solution until the detected potential becomes equal to the set potential. If the blended amount is larger than the desired value and iodine remains, the iodine molecule I with a value larger than the set potential of the control device is
The equilibrium potential of __2 and iodine ion I^- is detected using a gold or platinum electrode and a reference electrode, and the difference between this detected potential and the set potential becomes a signal, and formaldehyde is heated to the chemical copper plate until the detected potential becomes equal to the set potential. A method for controlling the concentration of a reducing agent in a chemical copper plating solution, characterized in that the plating solution is not replenished. 2 A pH buffering agent that exhibits a pH buffering effect at pH 6 to 12 is
The chemical copper plating solution according to claim 1, characterized in that it is potassium dihydrogen phosphate, disodium hydrogen phosphate, sodium carbonate, borax, sodium citrate, ammonium chloride, or sodium dimethylglycine. How to control the concentration of reducing agent inside. 3 A pH buffering agent that has a pH buffering effect at pH 2 to 9 is
A method for controlling the concentration of a reducing agent in a chemical copper plating solution according to claim 1, characterized in that potassium hydrogen citrate, potassium dihydrogen phosphate, sodium citrate, glycine, or potassium hydrogen phthalate is used. . 4 A device that mixes a certain volume of a chemical copper plating solution with a solution containing sulfite ions and a pH buffering agent that has a pH buffering effect in the pH range of 6 to 12, and a device that mixes a certain volume of a solution that contains sulfite ions and a pH buffering agent that has a pH buffering effect in the pH range of 6 to 12, and a device that mixes a certain volume of a solution that contains sulfite ions and a pH buffering agent that has a pH buffering effect in the pH range of 2 to 9.
A device that mixes a fixed volume of an aqueous solution containing a buffer, a device that detects the potential of this mixed solution, and if the detected potential is smaller than a preset potential, the potential difference becomes a signal and becomes the detected potential. The controller replenishes formaldehyde until the set potentials are equal, and if the detected potential is greater than the preset potential, the difference becomes a signal and stops formaldehyde replenishment until the detected potential becomes equal to the set potential. A device for controlling the concentration of a reducing agent in a chemical copper plating solution.
JP52064813A 1977-06-03 1977-06-03 Method and device for controlling reducing agent concentration in chemical copper plating solution Expired JPS6032820B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52064813A JPS6032820B2 (en) 1977-06-03 1977-06-03 Method and device for controlling reducing agent concentration in chemical copper plating solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52064813A JPS6032820B2 (en) 1977-06-03 1977-06-03 Method and device for controlling reducing agent concentration in chemical copper plating solution

Publications (2)

Publication Number Publication Date
JPS541093A JPS541093A (en) 1979-01-06
JPS6032820B2 true JPS6032820B2 (en) 1985-07-30

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP52064813A Expired JPS6032820B2 (en) 1977-06-03 1977-06-03 Method and device for controlling reducing agent concentration in chemical copper plating solution

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Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015187595A (en) * 2014-03-14 2015-10-29 株式会社島津製作所 analyzer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015187595A (en) * 2014-03-14 2015-10-29 株式会社島津製作所 analyzer

Also Published As

Publication number Publication date
JPS541093A (en) 1979-01-06

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