JP3064712B2 - Electroless plating equipment - Google Patents
Electroless plating equipmentInfo
- Publication number
- JP3064712B2 JP3064712B2 JP4347164A JP34716492A JP3064712B2 JP 3064712 B2 JP3064712 B2 JP 3064712B2 JP 4347164 A JP4347164 A JP 4347164A JP 34716492 A JP34716492 A JP 34716492A JP 3064712 B2 JP3064712 B2 JP 3064712B2
- Authority
- JP
- Japan
- Prior art keywords
- electroless plating
- plating solution
- temperature
- electroless
- gas
- 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
Landscapes
- Chemically Coating (AREA)
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
られる無電解メッキ装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electroless plating apparatus used in the field of surface treatment.
【0002】[0002]
【従来の技術】従来より無電解メッキでは、無電解メッ
キ液槽内の無電解メッキ液の濃度分布のバラツキをなく
し、均一な無電解メッキを施すために、各種の攪拌操作
が行われている。例えば、特開昭54−121233、
特開昭59−161895に開示されている、気体の吹
き込みによる攪拌が挙げられる。さらに、特開昭63−
312983において、メッキ反応の進行に伴って無電
解メッキ液中の溶存酸素の濃度が低下するので、溶存酸
素の補給のために微細分化した酸素を含む気体を無電解
メッキ液に吹き込む方法が開示されている。2. Description of the Related Art Conventionally, in electroless plating, various stirring operations have been performed in order to eliminate variation in the concentration distribution of the electroless plating solution in the electroless plating solution tank and to perform uniform electroless plating. . For example, Japanese Patent Application Laid-Open No. 54-123233,
Stirring by blowing gas disclosed in JP-A-59-161895 can be mentioned. Further, JP-A-63-
No. 312983 discloses a method in which a gas containing finely divided oxygen is blown into the electroless plating solution to replenish the dissolved oxygen because the concentration of dissolved oxygen in the electroless plating solution decreases as the plating reaction proceeds. ing.
【0003】しかし、従来の無電解メッキ法における無
電解メッキ液中の溶存酸素濃度の制御によると、無電解
メッキ液の品質の安定が十分とはいえず、無電解メッキ
液の老朽化の進行度合いにばらつきがある。従って、長
時間にわたり被メッキ物のメッキ被膜の析出が安定した
無電解メッキ法が求められている。However, according to the control of the dissolved oxygen concentration in the electroless plating solution in the conventional electroless plating method, the stability of the quality of the electroless plating solution cannot be said to be sufficient, and the aging of the electroless plating solution has progressed. The degree varies. Therefore, there is a need for an electroless plating method in which the deposition of a plating film on an object to be plated is stable for a long time.
【0004】従来の無電解メッキ液の品質の不安定化
は、外気の温度が低い際に短時間で生じやすい。すなわ
ち、供給された気体の酸素はメッキ液に溶解する際、酸
素のメッキ液への溶解速度が低下し、その結果、被メッ
キ物へのメッキ被膜の析出をばらつがせると推測され
る。The instability of the quality of the conventional electroless plating solution tends to occur in a short time when the temperature of the outside air is low. That is, when the supplied gaseous oxygen dissolves in the plating solution, the rate of dissolution of oxygen in the plating solution is reduced, and as a result, it is assumed that the deposition of the plating film on the object to be plated varies.
【0005】[0005]
【発明が解決しようとする課題】本発明は上記の欠点を
解消するためになされたもので、その目的とするところ
は、外気の影響を受けることなく、長時間にわたり被メ
ッキ物のメッキ被膜の析出量を安定させる無電解メッキ
装置を提供することにある。SUMMARY OF THE INVENTION The present invention has been made in order to solve the above-mentioned drawbacks, and an object of the present invention is to provide a plating film for an object to be plated for a long time without being affected by the outside air. An object of the present invention is to provide an electroless plating apparatus that stabilizes the amount of deposition.
【0006】[0006]
【課題を解決するための手段】本発明の請求項1に係る
無電解メッキ装置は、無電解メッキ液の酸素溶解槽(1
3)を有する無電解メッキ装置で、酸素を含む気体を保
存又は取り入れる供給機(12)、上記気体の温度を検
出する検出装置と、この検出した信号に基づいて上記気
体の温度を30℃以上から無電解メッキの液温以下迄の
温度範囲となるよう指示信号を送るコントローラ
(6)、このコントローラ(6)からの指示信号に基づ
いて気体の温度を調節する温度調整器(5)、この温度
調整器(5)において所定の温度となった気体を、上記
酸素溶解槽(13)の無電解メッキ液に散気する散気管
(4)を備えていることを特徴とする。According to a first aspect of the present invention, there is provided an electroless plating apparatus comprising an oxygen dissolving tank (1) for an electroless plating solution.
A supply device (12) for storing or taking in a gas containing oxygen, a detection device for detecting the temperature of the gas, and a temperature of the gas of 30 ° C. or more based on the detected signal. A controller (6) for sending an instruction signal so that the temperature is within a range from the temperature of the electroless plating solution to below the temperature of the electroless plating; a temperature controller (5) for adjusting the temperature of the gas based on the instruction signal from the controller (6); A gas diffuser (4) for diffusing gas, which has reached a predetermined temperature in the temperature controller (5), into the electroless plating solution in the oxygen dissolving tank (13) is provided.
【0007】[0007]
【作用】本発明に係る無電解メッキ法は、供給する酸素
を含む気体温度を、30℃〜無電解メッキの液温の温度
範囲に限定することにより、無電解メッキ液中への酸素
の溶解量が安定するので、長時間にわたりメッキ被膜が
安定して析出する。According to the electroless plating method of the present invention, the temperature of the gas containing oxygen to be supplied is limited to a temperature range of 30 ° C. to the temperature of the electroless plating solution, thereby dissolving oxygen in the electroless plating solution. Since the amount is stable, the plating film is stably deposited for a long time.
【0008】酸素を含む気体は、気体を保存又は採り入
れる供給機(12)、上記気体の温度を検出する検出装
置と、この検出した信号に基づいて気体の温度を30℃
〜無電解メッキの液温の温度範囲となるよう指示信号を
送るを発信機を備えたコントローラ(6)、このコント
ローラ(6)からの指示信号に基づいて気体の温度を調
節する温度調整器(5)、この温度調整器(5)で所定
の温度となった気体を、無電解メッキ液槽(1)および
/または酸素溶解槽(13)の無電解メッキ液に散気す
る散気管(4)により無電解メッキ液に供給される。そ
の結果、長時間にわたり被メッキ物のメッキ被膜が安定
して析出する。The gas containing oxygen is supplied by a supply device (12) for storing or taking in the gas, a detecting device for detecting the temperature of the gas, and a gas temperature of 30 ° C. based on the detected signal.
A controller (6) having a transmitter for sending an instruction signal so as to be in a temperature range of the electroless plating solution temperature, and a temperature controller (6) for adjusting the gas temperature based on the instruction signal from the controller (6). 5) A diffuser pipe (4) for diffusing the gas which has reached a predetermined temperature in the temperature controller (5) into the electroless plating solution in the electroless plating solution tank (1) and / or the oxygen dissolving tank (13). ) Is supplied to the electroless plating solution. As a result, the plating film of the object to be plated is stably deposited for a long time.
【0009】以下、本発明を詳細に説明する。Hereinafter, the present invention will be described in detail.
【0010】本発明の無電解メッキ装置を図1〜2に基
づいて説明する。An electroless plating apparatus according to the present invention will be described with reference to FIGS.
【0011】図1は本発明の参考例に係る無電解メッキ
装置のブロック図であり、図2は実施例に係る無電解メ
ッキ装置のブロック図である。FIG. 1 is a block diagram of an electroless plating apparatus according to a reference example of the present invention, and FIG. 2 is a block diagram of an electroless plating apparatus according to the embodiment.
【0012】図1に示す無電解メッキ装置は、無電解メ
ッキ液槽(1)は、無電解メッキ液が満たされ、被メッ
キ物(3)を無電解メッキ液中に浸漬して無電解メッキ
を施すものである。無電解メッキ装置は、酸素を含む気
体を保存又は採り入れる供給機(12)を備える。上記
供給機(12)としては、例えば上記気体が酸素の場合
は酸素ボンベ、上記気体が空気の場合は送風機等が挙げ
られる。さらに、上記気体の温度を検出する検出装置
と、この検出した信号に基づいて気体の温度を30℃〜
無電解メッキの液温の温度範囲となるよう指示信号を送
るコントローラ(6)、このコントローラ(6)からの
指示信号に基づいて気体の温度を調節する温度調整器
(5)を備える。この温度調整器(5)としては、例え
ば気体の加温のみであればヒータが挙げられる。そし
て、所望の温度となった上記気体を、無電解メッキ液槽
(1)の無電解メッキ液に散気する散気管(4)を備え
る。この散気管(4)としては、上記気体中の酸素を微
細分化して無電解メッキ液に溶解させるために、例え
ば、中空多孔質のフッソ樹脂製散気管、中空多孔質のセ
ラミック製散気管が挙げられる。上記散気管(4)は被
メッキ物(3)の下方に備える方が、無電解メッキ液へ
の酸素溶解の効率を高め、無電解メッキ液槽(1)内の
無電解メッキ液の濃度分布のばらつきを少なくするので
好ましい。また、必要に応じて、上記温度調整器(5)
で温度を調節した気体の供給量を調整する弁(7)、こ
の弁(7)を通過した気体の供給量を測定する流量計
(8)を温度調整器(5)と無電解メッキ液槽(1)の
間に備える。In the electroless plating apparatus shown in FIG. 1, an electroless plating solution tank (1) is filled with an electroless plating solution, and an object to be plated (3) is immersed in the electroless plating solution. Is applied. The electroless plating apparatus includes a supply device (12) for storing or taking in a gas containing oxygen. Examples of the supply device (12) include an oxygen cylinder when the gas is oxygen, and a blower when the gas is air. Further, a detecting device for detecting the temperature of the gas, and a temperature of the gas of 30 ° C. or more based on the detected signal.
A controller (6) for sending an instruction signal so as to be in a temperature range of the electroless plating solution temperature, and a temperature controller (5) for adjusting a gas temperature based on the instruction signal from the controller (6). As the temperature controller (5), for example, a heater may be used if only gas is heated. Further, there is provided a diffuser pipe (4) for diffusing the gas at a desired temperature into the electroless plating solution in the electroless plating solution tank (1). As the air diffuser (4), for example, in order to finely differentiate oxygen in the gas and dissolve it in the electroless plating solution, for example, a hollow porous fluororesin diffuser or a hollow porous ceramic diffuser is used. No. Providing the air diffusion tube (4) below the object to be plated (3) enhances the efficiency of dissolving oxygen in the electroless plating solution and increases the concentration distribution of the electroless plating solution in the electroless plating solution tank (1). This is preferable because the variation in is reduced. In addition, if necessary, the temperature controller (5)
A valve (7) for adjusting the supply amount of the gas whose temperature has been adjusted by (1), a flow meter (8) for measuring the supply amount of the gas passing through the valve (7), a temperature controller (5) and an electroless plating solution tank Prepare during (1).
【0013】本発明の無電解メッキ装置は図2に示す如
く、上記気体を散気する散気管(4)を無電解メッキ液
槽(1)内に代わり、酸素溶解槽(13)内に備え、無
電解メッキ液を無電解メッキ液槽(1)と酸素溶解槽
(13)の間を循環させるポンプ(14)、および循環
用配管(15)を備える。As shown in FIG. 2, the electroless plating apparatus of the present invention is provided with an air diffusion tube (4) for diffusing the gas in an oxygen dissolution tank (13) instead of the electroless plating solution tank (1). A pump (14) for circulating the electroless plating solution between the electroless plating solution tank (1) and the oxygen dissolving tank (13), and a circulation pipe (15).
【0014】次に無電解メッキ法について図1に基づい
て説明する。Next, the electroless plating method will be described with reference to FIG.
【0015】上記無電解メッキ液槽(1)には、メッキ
を施すための無電解メッキ液が満たされている。この無
電解メッキ液は公知の各種無電解メッキ液が用いられ、
例えば無電解銅メッキ、無電解ニッケルメッキが挙げら
れる。上記メッキ液の温度は一般に50℃〜90℃に保
持される。The electroless plating solution tank (1) is filled with an electroless plating solution for plating. As this electroless plating solution, various known electroless plating solutions are used,
Examples include electroless copper plating and electroless nickel plating. The temperature of the plating solution is generally maintained at 50 ° C to 90 ° C.
【0016】上記においては、酸素ボンベや送風機等の
供給機(12)を用い酸素を含む気体を保存又は採り入
れる。上記気体の温度はコントローラ(6)内に備えら
れた検出装置で検出し、この検出した信号に基づいて気
体の温度を30℃〜無電解メッキの液温の温度範囲とな
るよう温度調整器(5)へ指示信号を送る。このコント
ローラ(6)からの指示信号に基づいて温度調整器
(5)で、気体の温度を所定の温度に調節する。また、
必要に応じて上記温度を調節した気体を、弁(7)の開
閉度合いを調整し気体の供給量が流量計(8)で一定と
する。In the above, a gas containing oxygen is stored or taken in using a supply device (12) such as an oxygen cylinder or a blower. The temperature of the gas is detected by a detection device provided in the controller (6), and based on the detected signal, the temperature of the gas is adjusted to a temperature range of 30 ° C. to the temperature of the electroless plating solution. Send an instruction signal to 5). The temperature of the gas is adjusted to a predetermined temperature by the temperature controller (5) based on the instruction signal from the controller (6). Also,
If necessary, the temperature of the gas is adjusted, and the opening / closing degree of the valve (7) is adjusted so that the gas supply amount is kept constant by the flow meter (8).
【0017】そして、所望の温度となった上記気体は、
無電解メッキ液槽(1)に備えられた散気管(4)よ
り、無電解メッキ液中に散気される。上記散気される酸
素を含む気体が、30℃〜無電解メッキの液温の温度範
囲なので、上記無電解メッキ液の温度が低下しないの
で、従って酸素の無電解メッキ液への溶解速度を低下す
ることがなく、長時間にわたりメッキ被膜の析出量を安
定させる。Then, the gas having reached a desired temperature is
The gas is diffused into the electroless plating solution from a diffuser tube (4) provided in the electroless plating solution tank (1). Since the gas containing oxygen to be diffused is in the temperature range of 30 ° C. to the temperature of the electroless plating solution, the temperature of the electroless plating solution does not decrease. Therefore, the dissolution rate of oxygen in the electroless plating solution is reduced. And stabilizes the deposition amount of the plating film over a long period of time.
【0018】本発明の無電解メッキ法として、図2に示
す如く、散気管(4)を無電解メッキ液槽(1)内に代
わり、酸素溶解槽(13)内に備えて、酸素溶解槽(1
3)内のメッキ液に30℃〜無電解メッキの液温の温度
範囲の酸素を含む気体を散気し、上記酸素溶解槽(1
3)内の無電解メッキ液と無電解メッキ液槽(1)内の
無電解メッキ液を循環させる方法がある。上記酸素溶解
槽(13)を設けると、酸素溶解槽(13)内で所望の
溶存酸素濃度に調整した無電解メッキ液を無電解メッキ
液槽(1)に送るので、気体を直接被メッキ物(3)に
当てたくない場合に有用である。According to the electroless plating method of the present invention, as shown in FIG. 2, an air diffusion tube (4) is provided in an oxygen dissolution tank (13) instead of the electroless plating solution tank (1). (1
A gas containing oxygen in the temperature range of 30 ° C. to the electroless plating solution temperature is diffused into the plating solution in 3), and the oxygen dissolving tank (1) is diffused.
There is a method of circulating the electroless plating solution in 3) and the electroless plating solution in the electroless plating solution tank (1). When the oxygen dissolving tank (13) is provided, the electroless plating solution adjusted to a desired dissolved oxygen concentration in the oxygen dissolving tank (13) is sent to the electroless plating solution tank (1), so that the gas is directly transferred to the plating object. This is useful when you do not want to apply (3).
【0019】また、本発明において、無電解メッキ液槽
(1)の無電解メッキ液は、金属イオン濃度、還元剤の
濃度、pH値等を測定し、メッキ反応に伴って変化する
無電解メッキ液の組成を維持するため、新たに金属イオ
ン化合物、金属イオンの還元剤、pH調整剤を適宜無電
解メッキ液に補給する。In the present invention, the electroless plating solution in the electroless plating solution tank (1) measures the concentration of a metal ion, the concentration of a reducing agent, the pH value, etc., and changes the electroless plating solution with the plating reaction. In order to maintain the composition of the solution, a metal ion compound, a reducing agent for the metal ion, and a pH adjuster are newly supplied to the electroless plating solution as appropriate.
【0020】[0020]
【実施例】参考例1 図1に示す無電解メッキ装置を用いて無電解銅メッキを
行った。無電解メッキ液槽(1)に下記無電解銅メッキ
液を満たした。なお、この無電解銅メッキ液にpH調整
剤として水酸化ナトリウムを加え、pHを測定したとこ
ろpHは12.0であった。被メッキ物(3)として銅
板をこの無電解銅メッキ液に浸漬した。無電解メッキ液
槽(1)中の無電解銅メッキ液の銅イオン濃度、ホルマ
リン濃度、pH値を測定し、メッキ反応に伴い、上記濃
度やpHが一定となるよう銅イオン、ホルマリン、水酸
化ナトリウムを補給した。EXAMPLES Reference Example 1 Electroless copper plating was performed using the electroless plating apparatus shown in FIG. The electroless plating solution tank (1) was filled with the following electroless copper plating solution. In addition, sodium hydroxide was added to this electroless copper plating solution as a pH adjuster, and the pH was measured to be 12.0. A copper plate was immersed in the electroless copper plating solution as a plating object (3). The copper ion concentration, formalin concentration, and pH value of the electroless copper plating solution in the electroless plating solution tank (1) are measured, and the copper ion, formalin, and hydroxide are adjusted so that the above-mentioned concentration and pH become constant with the plating reaction. Supplemented with sodium.
【0021】無電解銅メッキ液の条件 ・硫酸銅−−−−−−−−−−10g/リットル ・EDTA−−−−−−−−−30g/リットル ・ホルマリン−−−−−−−− 5g/リットル ・シアン系添加剤−−−−−−10mg/リットル ・ポリエチレングリコール−−200mg/リットル ・pH−−−−−−−−−−−12.0 ・液温−−−−−−−−−−−60℃ 酸素を含む気体は、供給機(12)である酸素ボンベの
酸素を用いた。上記酸素の温度を、コントローラ(6)
内に備えられた検出装置で検出した信号に基づいて酸素
を40±5℃となるよう温度調整器(5)で加温した。
多孔性フッソ樹脂製の散気管(4)を無電解メッキ液槽
(1)の底に設け、上記酸素を無電解メッキ液槽(1)
内の無電解メッキ液に散気した。メッキ処理中の無電解
メッキ液の溶存酸素濃度は1ppmの一定値に保持でき
た。Conditions for the electroless copper plating solution: Copper sulfate --------------- 10 g / liter EDTA--30 g / liter -Formalin --------- 5g / liter ・ Cyanide additive --10mg / liter ・ Polyethylene glycol -200mg / liter ・ pH --------------- 12.0 ・ Liquid temperature ---- −−−−− 60 ° C. As the gas containing oxygen, oxygen from an oxygen cylinder as the supply device (12) was used. The temperature of the oxygen is controlled by the controller (6).
Oxygen was heated by a temperature controller (5) to 40 ± 5 ° C. based on a signal detected by a detection device provided therein.
A diffuser tube (4) made of porous fluororesin is provided at the bottom of the electroless plating solution tank (1), and the oxygen is supplied to the electroless plating solution tank (1).
The inside of the electroless plating solution was diffused. The dissolved oxygen concentration of the electroless plating solution during the plating process could be maintained at a constant value of 1 ppm.
【0022】その結果、メッキの老朽化度を示す15タ
ーンまで無電解銅メッキを行ったが、無電解メッキ液槽
(1)内への銅の析出はなく、この間被メッキ物(3)
表面のメッキ被膜の析出は良好であった。As a result, the electroless copper plating was performed up to 15 turns indicating the aging degree of the plating. However, no copper was deposited in the electroless plating solution tank (1), and during this time, the plating object (3)
The deposition of the plating film on the surface was good.
【0023】参考例2参考 例1の酸素を含む気体を、酸素ボンベの酸素に代わ
り、空気を用い供給機(12)である送風機で取り入れ
た以外は、参考例1と同様の無電解銅メッキ条件、気体
の温度で実施した。 REFERENCE EXAMPLE 2 The same electroless copper plating as in Reference Example 1 except that the gas containing oxygen of Reference Example 1 was introduced by a blower as a supply unit (12) using air instead of oxygen in an oxygen cylinder. The test was carried out under the conditions of gas temperature.
【0024】その結果、メッキの老朽化度を示す15タ
ーンまで無電解銅メッキを行ったが、無電解メッキ液槽
(1)内への銅の析出はなく、この間被メッキ物(3)
表面のメッキ被膜の析出は良好であった。As a result, the electroless copper plating was performed up to 15 turns indicating the aging degree of the plating. However, no copper was deposited in the electroless plating solution tank (1).
The deposition of the plating film on the surface was good.
【0025】参考例3参考 例1と同様の無電解メッキ装置を用いて、無電解ニ
ッケルメッキを行った。無電解メッキ液槽(1)に下記
の無電解ニッケルメッキ液を満たし、被メッキ物(3)
として銅板に無電解ニッケルメッキを施した。無電解メ
ッキ液槽(1)中の無電解ニッケルメッキ液のニッケル
イオン濃度、次亜りん酸ナトリウム濃度、pH値を測定
し、メッキ反応に伴い、上記濃度やpHが一定となるよ
うニッケルイオン、次亜りん酸ナトリウム、水酸化ナト
リウム又は硫酸を補給した。 Reference Example 3 Electroless nickel plating was performed using the same electroless plating apparatus as in Reference Example 1. The electroless plating solution tank (1) is filled with the following electroless nickel plating solution, and the object to be plated (3)
The copper plate was subjected to electroless nickel plating. The nickel ion concentration, sodium hypophosphite concentration, and pH value of the electroless nickel plating solution in the electroless plating solution tank (1) were measured, and nickel ions were added so that the concentration and pH became constant with the plating reaction. Supplemented with sodium hypophosphite, sodium hydroxide or sulfuric acid.
【0026】無電解ニッケルメッキ液の条件 ・硫酸ニッケル六水和物−−−−−−−30g/リットル ・次亜りん酸ナトリウム−−−−−−−30g/リットル ・グリシン−−−−−−−−−−−−−20g/リットル ・クエン酸ナトリウム−−−−−−−−20g/リットル ・鉛系添加剤−−−−−−−−−−−−10mg/リットル ・pH−−−−−−−−−−−−−−−5.5 ・液温−−−−−−−−−−−−−−−90℃ 酸素を含む気体は空気を用い、供給機(12)である送
風機で取り入れた。上記空気の温度を、コントローラ
(6)内に備えられた検出装置で検出した信号に基づい
て空気を60±5℃となるよう温度調整器(5)で加温
した。多孔性フッソ樹脂製の散気管(4)を無電解メッ
キ液槽(1)の底に設け、上記空気を無電解メッキ液槽
(1)内の無電解ニッケルメッキ液に散気した。メッキ
処理中の無電解ニッケルメッキ液の溶存酸素濃度は0.
5ppmの一定値に保持できた。Conditions for electroless nickel plating solution Nickel sulfate hexahydrate 30 g / liter Sodium hypophosphite 30 g / liter Glycine 20 g / l sodium citrate 20 g / l lead-based additive 10 mg / l pH- −−−−−−−−−−−−−− 5.5 liquid temperature −−−−−−−−−−−−− 90 ° C. The gas containing oxygen uses air, and the feeder (12) Was taken in by a blower. The temperature of the air was heated by a temperature controller (5) to 60 ± 5 ° C. based on a signal detected by a detection device provided in the controller (6). A diffuser tube (4) made of porous fluororesin was provided at the bottom of the electroless plating solution tank (1), and the air was diffused into the electroless nickel plating solution in the electroless plating solution tank (1). The dissolved oxygen concentration of the electroless nickel plating solution during the plating process is 0.1.
It could be kept at a constant value of 5 ppm.
【0027】その結果、メッキの老朽化度を示す12タ
ーンまで無電解ニッケルメッキを行ったが、無電解メッ
キ液槽(1)内へのニッケルの析出はなく、この間被メ
ッキ物(3)表面のメッキ被膜の析出は良好であった。As a result, electroless nickel plating was performed up to 12 turns indicating the aging degree of the plating. However, no nickel was deposited in the electroless plating solution tank (1). The deposition of the plating film was good.
【0028】実施例1 図2に示す無電解メッキ装置を用いて無電解銅メッキを
おこなった。無電解銅メッキの条件、被メッキ物(3)
は参考例1と同一のものを用いた。Example 1 Electroless copper plating was performed using an electroless plating apparatus shown in FIG. Conditions for electroless copper plating, plating object (3)
Was the same as in Reference Example 1.
【0029】酸素を含む気体は空気を用い、供給機(1
2)である送風機で取り入れた。上記空気の温度を、コ
ントローラ(6)内に備えられた検出装置で検出した信
号に基づいて空気を40±5℃となるよう温度調整器
(5)で加温した。The gas containing oxygen uses air, and the feeder (1
2) was taken in by the blower. The temperature of the air was heated by the temperature controller (5) to 40 ± 5 ° C. based on a signal detected by a detection device provided in the controller (6).
【0030】酸素溶解槽(13)の底に多孔性フッソ樹
脂製の散気管(4)を備え、上記空気を酸素溶解槽(1
3)内の無電解メッキ液に散気管(4)から散気した。
配管(15)に備えたポンプ(14)を作動し、上記酸
素溶解槽(13)内の無電解メッキ液を無電解メッキ液
槽(1)内に送り、他の配管(16)で無電解メッキ液
槽(1)内の無電解メッキ液を酸素溶解槽(13)内に
戻し、酸素溶解槽(13)と無電解メッキ液槽(1)の
無電解メッキ液を循環した。メッキ処理中の無電解メッ
キ液槽(1)内の無電解銅メッキ液の溶存酸素濃度は1
ppmの一定値に保持できた。An air diffusion tube (4) made of porous fluororesin is provided at the bottom of the oxygen dissolution tank (13), and the air is supplied to the oxygen dissolution tank (1).
Air was diffused from the diffuser tube (4) to the electroless plating solution in 3).
The pump (14) provided in the pipe (15) is operated, and the electroless plating solution in the oxygen dissolving tank (13) is sent to the electroless plating solution tank (1), and the electroless plating liquid is electrolessly supplied to another pipe (16). The electroless plating solution in the plating solution tank (1) was returned to the oxygen dissolving tank (13), and the electroless plating solution in the oxygen dissolving tank (13) and the electroless plating solution tank (1) was circulated. The concentration of dissolved oxygen in the electroless copper plating solution in the electroless plating solution tank (1) during plating is 1
ppm could be maintained at a constant value.
【0031】その結果、メッキの老朽化度を示す15タ
ーンまで無電解銅メッキを行ったが、無電解メッキ液槽
(1)内への銅の析出はなく、この間被メッキ物(3)
表面のメッキ被膜の析出は良好であった。As a result, the electroless copper plating was performed up to 15 turns indicating the aging degree of the plating. However, no copper was deposited in the electroless plating solution tank (1).
The deposition of the plating film on the surface was good.
【0032】比較例1参考 例2の空気の温度を20±5℃とした以外は参考例
2と同様にして無電解銅メッキを行った。メッキ処理中
の無電解メッキ液槽(1)内の無電解銅メッキ液の溶存
酸素濃度は0.3ppmと実施例と比較して少なかっ
た。Comparative Example 1 Electroless copper plating was performed in the same manner as in Reference Example 2 except that the temperature of the air in Reference Example 2 was changed to 20 ± 5 ° C. The dissolved oxygen concentration of the electroless copper plating solution in the electroless plating solution tank (1) during the plating process was 0.3 ppm, which was lower than that of the example.
【0033】その結果、メッキの老朽化度を示す11タ
ーンで、無電解メッキ液槽(1)内に銅の析出を生じ
た。As a result, copper deposition occurred in the electroless plating solution tank (1) in 11 turns indicating the aging degree of plating.
【0034】[0034]
【発明の効果】本発明の無電解メッキ装置を用いると、
外気の影響を受けることなく、長時間にわたり被メッキ
物のメッキ被膜の析出を良好にする。According to the electroless plating apparatus of the present invention,
It is possible to improve the deposition of a plating film on an object to be plated for a long time without being affected by the outside air.
【図1】本発明の参考例に係る無電解メッキ装置のブロ
ック図である。FIG. 1 is a block diagram of an electroless plating apparatus according to a reference example of the present invention.
【図2】本発明の一実施例に係る無電解メッキ装置のブ
ロック図である。FIG. 2 is a block diagram of an electroless plating apparatus according to one embodiment of the present invention.
1 無電解メッキ液槽 3 被メッキ物 4 散気管 5 温度調整器 6 コントローラ 7 弁 8 流量計 12 供給機 13 酸素溶解槽 14 ポンプ 15 配管 DESCRIPTION OF SYMBOLS 1 Electroless plating solution tank 3 Plated object 4 Air diffuser 5 Temperature controller 6 Controller 7 Valve 8 Flow meter 12 Feeder 13 Oxygen dissolving tank 14 Pump 15 Piping
───────────────────────────────────────────────────── フロントページの続き (72)発明者 吉井 靖 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4−157170(JP,A) 特開 昭63−69999(JP,A) (58)調査した分野(Int.Cl.7,DB名) C23C 18/00 - 18/54 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Yasushi Yoshii 1048 Odakadoma, Kadoma City, Osaka Prefecture Matsushita Electric Works, Ltd. (56) References JP 4-157170 (JP, A) JP 63-69999 ( JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C23C 18/00-18/54
Claims (1)
有する無電解メッキ装置で、酸素を含む気体を保存又は
取り入れる供給機(12)、上記気体の温度を検出する
検出装置と、この検出した信号に基づいて上記気体の温
度を30℃以上から無電解メッキの液温以下迄の温度範
囲となるよう指示信号を送るコントローラ(6)、この
コントローラ(6)からの指示信号に基づいて気体の温
度を調節する温度調整器(5)、この温度調整器(5)
において所定の温度となった気体を、上記酸素溶解槽
(13)の無電解メッキ液に散気する散気管(4)を備
えていることを特徴とする無電解メッキ装置。An electroless plating apparatus having an oxygen dissolving tank (13) for an electroless plating solution, a supply device (12) for storing or taking in a gas containing oxygen, a detection device for detecting the temperature of the gas, A controller (6) that sends an instruction signal based on the detected signal so that the temperature of the gas is in a temperature range from 30 ° C. or more to a liquid temperature of electroless plating, and based on the instruction signal from the controller (6). Temperature controller (5) for adjusting the temperature of gas, this temperature controller (5)
The electroless plating apparatus according to claim 1, further comprising a diffuser pipe (4) for diffusing gas having a predetermined temperature into the electroless plating solution in the oxygen dissolving tank (13).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4347164A JP3064712B2 (en) | 1992-12-25 | 1992-12-25 | Electroless plating equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4347164A JP3064712B2 (en) | 1992-12-25 | 1992-12-25 | Electroless plating equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06280034A JPH06280034A (en) | 1994-10-04 |
JP3064712B2 true JP3064712B2 (en) | 2000-07-12 |
Family
ID=18388350
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4347164A Expired - Fee Related JP3064712B2 (en) | 1992-12-25 | 1992-12-25 | Electroless plating equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3064712B2 (en) |
-
1992
- 1992-12-25 JP JP4347164A patent/JP3064712B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH06280034A (en) | 1994-10-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4152467A (en) | Electroless copper plating process with dissolved oxygen maintained in bath | |
US9435041B2 (en) | Method and regeneration apparatus for regenerating a plating composition | |
US5182131A (en) | Plating solution automatic control | |
JP3064712B2 (en) | Electroless plating equipment | |
GB1588758A (en) | Method and apparatus for control of electroless plating solutions | |
EP0043893A1 (en) | Regulation of the plating solution in a plating bath | |
US4684545A (en) | Electroless plating with bi-level control of dissolved oxygen | |
US4616596A (en) | Electroless plating apparatus | |
US20090238979A1 (en) | Method of Applying Catalytic Solution for Use in Electroless Deposition | |
US6733679B2 (en) | Method of treating an electroless plating waste | |
JP2833393B2 (en) | Electroless copper plating method | |
US3982054A (en) | Method for electrolessly depositing metals using improved sensitizer composition | |
JPS60145379A (en) | Preparation of take mode electroless copper plating bath | |
JP3809608B2 (en) | Electroless copper plating method and apparatus, and copper replenisher preparation method and apparatus | |
JPH07316829A (en) | Electroless plating method | |
JPS5921386B2 (en) | Automatic plating speed control method for electroless plating | |
US4967690A (en) | Electroless plating with bi-level control of dissolved oxygen, with specific location of chemical maintenance means | |
JPH0361380A (en) | Electroless tin plating bath | |
JPH02159029A (en) | Chemical treatment and device therefor | |
JP2003301285A (en) | Method for circulating etchant and circulation tank | |
JP2684906B2 (en) | Electroless copper plating method on ceramic substrate | |
US6024922A (en) | Method of controlling an oxygen analyzer of the Hersch galvanic type | |
JPH03240969A (en) | Method for preserving copper ion replenishing solution for electroless copper plating | |
US4710224A (en) | Process for introducing bath components into electrolytic and currentless baths | |
JPH079067B2 (en) | Electroless copper plating method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |