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JP3038876B2 - Electroless copper plating bath stirring method - Google Patents
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JP3038876B2 - Electroless copper plating bath stirring method - Google Patents

Electroless copper plating bath stirring method

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Publication number
JP3038876B2
JP3038876B2 JP2281342A JP28134290A JP3038876B2 JP 3038876 B2 JP3038876 B2 JP 3038876B2 JP 2281342 A JP2281342 A JP 2281342A JP 28134290 A JP28134290 A JP 28134290A JP 3038876 B2 JP3038876 B2 JP 3038876B2
Authority
JP
Japan
Prior art keywords
nitrogen gas
air
pipe
plating
dissolved oxygen
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 - Lifetime
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JP2281342A
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Japanese (ja)
Other versions
JPH04157170A (en
Inventor
朝夫 村上
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 Corp
Original Assignee
NEC Corp
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Filing date
Publication date
Application filed by NEC Corp filed Critical NEC Corp
Priority to JP2281342A priority Critical patent/JP3038876B2/en
Publication of JPH04157170A publication Critical patent/JPH04157170A/en
Application granted granted Critical
Publication of JP3038876B2 publication Critical patent/JP3038876B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、電気絶縁物質を触媒液で活性化し、該電気
絶縁物質の表面に無電解銅めっきにより金属被覆を行う
無電解銅めっき浴の撹拌方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an electroless copper plating bath which activates an electric insulating material with a catalyst solution and coats the surface of the electric insulating material with metal by electroless copper plating. It relates to a stirring method.

〔従来の技術〕[Conventional technology]

一般に電子工業においては、プラスチック素材の表面
を無電解めっきにより金属被覆し、導電化することが広
く行われている。例えば、印刷配線板の製造において
は、銅張りエポキシ樹脂積層板の表面の所望の位置に貫
通孔を形成した後、貫通孔壁に触媒液を吸着させ、次い
で無電解銅めっきにより貫通孔壁面に金属被覆を施し、
貫通孔壁面を導電化することが行われている。
Generally, in the electronics industry, the surface of a plastic material is widely covered with metal by electroless plating to make it conductive. For example, in the production of a printed wiring board, after forming a through hole at a desired position on the surface of a copper-clad epoxy resin laminate, a catalyst solution is adsorbed on the through hole wall, and then the through hole wall is formed by electroless copper plating. Apply metal coating,
Making the wall surface of the through hole conductive has been performed.

従来、無電解銅めっき浴の撹拌方法としては、空気撹
拌が広く使用されている。この空気撹拌方法は、第3図
(a)に示すように、めっき槽4の内底部に、相互に連
通したパイプ6,6…を並列に配列し、各パイプ6の上周
面に開口した空気吹出口より空気をめっき槽4に吹出し
て触媒液を撹拌するものであり、この空気撹拌方法によ
れば、めっき槽4でのめっき中の空気撹拌が浴中の溶存
酸素濃度を安定化させ、これにより浴を分解させずに安
定に保つことができ、また正常なめっき反応を進行する
ことができるという利点がある。
Conventionally, air stirring has been widely used as a stirring method for an electroless copper plating bath. In this air stirring method, as shown in FIG. 3 (a), mutually connected pipes 6, 6,... Are arranged in parallel on the inner bottom of the plating tank 4, and each pipe 6 is opened on the upper peripheral surface. Air is blown out from the air outlet into the plating tank 4 to stir the catalyst solution. According to this air stirring method, air stirring during plating in the plating tank 4 stabilizes the dissolved oxygen concentration in the bath. Thus, there is an advantage that the bath can be kept stable without being decomposed, and a normal plating reaction can proceed.

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

上述した従来の無電解銅めっき浴撹拌方法では、溶存
酸素濃度を浴が不活性にならない程度の安定した状態に
保たなければならないために、以下のような欠点を有す
る。すなわち、 (1) めっき液建浴直後は、溶存酸素濃度が飽和に達
しているため、無電解銅めっき液が不活性であるため
に、第3図(b)に示すように、空気撹拌を行わない状
態でダミー板5を投入することにより、溶存酸素濃度を
数時間かけて低下させ、めっき液を活性化させなければ
ならない。このため、サイクルタイムにより順次製品を
投入する薄付け無電解銅めっきラインでは、数サイクル
のダミー投入が必要となり、無駄なコストを発生する。
The conventional electroless copper plating bath stirring method described above has the following disadvantages because the dissolved oxygen concentration must be maintained in a stable state that does not render the bath inactive. (1) Immediately after the bathing of the plating solution, the dissolved oxygen concentration has reached saturation, and the electroless copper plating solution is inactive. Therefore, as shown in FIG. By introducing the dummy plate 5 in a state where the plating is not performed, the concentration of dissolved oxygen must be reduced over several hours to activate the plating solution. For this reason, in a thin electroless copper plating line in which products are sequentially supplied according to the cycle time, several cycles of dummy input are required, and wasteful costs are generated.

(2) 空気撹拌の通気量を一定に設定した場合、溶存
酸素濃度を一定量で安定化させるためには、投入する被
めっき物のロードファクターを一定にしなければならな
い。
(2) When the air flow rate of the air stirring is set to be constant, in order to stabilize the dissolved oxygen concentration at a constant amount, the load factor of the object to be plated must be constant.

等の欠点があった。And the like.

本発明の目的はめっき槽内の溶存酸素濃度の制御を行
う無電解銅めっき浴撹拌方法を提供することにある。
An object of the present invention is to provide an electroless copper plating bath stirring method for controlling the concentration of dissolved oxygen in a plating tank.

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

前記目的を達成するため、本発明に係る無電解銅めっ
き浴攪拌方法は、ガス吹出工程と、濃度制御工程とを有
し、めっき槽内のめっき液を攪拌する無電解銅めっき浴
攪拌方法であって、 前記ガス吹出工程は、一つのめっき槽内の内底面中央
部に配設された窒素ガス配管とこの外周を取り囲むよう
に配設された空気配管とのそれぞれの上方の領域内に、
窒素ガス配管から窒素ガスを、空気配管から空気を吹出
して、窒素ガスと空気とを併用してめっき液のガス攪拌
を行う工程であり、 前記濃度制御工程は、前記窒素ガス配管と前記空気配
管とのそれぞれの上方の領域内に対応して、めっき槽内
の中央部に窒素ガスによる溶存酸素低濃度領域とめっき
槽の内側面に接して空気による溶存酸素高濃度領域との
異なる二つの領域を一つのめっき槽内に形成する工程で
ある。
In order to achieve the above object, an electroless copper plating bath stirring method according to the present invention includes a gas blowing step and a concentration control step, and is an electroless copper plating bath stirring method for stirring a plating solution in a plating tank. The gas blowing step is performed in a region above each of a nitrogen gas pipe disposed at the center of the inner bottom surface in one plating tank and an air pipe disposed to surround the outer periphery.
Nitrogen gas is blown out of the nitrogen gas pipe, air is blown out of the air pipe, and the gas is stirred in the plating solution using the nitrogen gas and the air together. The concentration control step is performed by the nitrogen gas pipe and the air pipe. Two different regions corresponding to the upper region of each of the above, corresponding to a dissolved oxygen low concentration region by nitrogen gas in the center part of the plating tank and a dissolved oxygen high concentration region by air in contact with the inner surface of the plating tank. Is formed in one plating tank.

〔作用〕[Action]

空気と窒素ガスとによりガス撹拌し、めっき槽内の溶
存酸素濃度の制御を行い、この制御によりめっき槽内に
溶存酸素濃度の高い領域と低い領域を作り出す。
Gas stirring is performed with air and nitrogen gas to control the dissolved oxygen concentration in the plating tank, and by this control, a region having a high and low dissolved oxygen concentration is created in the plating tank.

〔実施例〕〔Example〕

以下、本発明を図面を参照して説明する。 Hereinafter, the present invention will be described with reference to the drawings.

(実施例1) 第1図は、本発明の一実施例の無電解銅めっき浴撹拌
方法を用いためっき槽を示す斜視図である。
(Example 1) Fig. 1 is a perspective view showing a plating tank using an electroless copper plating bath stirring method according to one example of the present invention.

図において、窒素ガス配管1は、並列に配列した横パ
イプ1a,1a…と、複数のパイプ1a,1a…の両端を相互に連
通した縦パイプ1b,1bとを組合せてなるもので、窒素ガ
ス配管1は、めっき槽3の内底面の中央部分に設置され
ている。
In the figure, a nitrogen gas pipe 1 is a combination of horizontal pipes 1a, 1a ... arranged in parallel and vertical pipes 1b, 1b communicating both ends of a plurality of pipes 1a, 1a ... The pipe 1 is provided at the center of the inner bottom surface of the plating tank 3.

空気配管2は、窒素ガス配管1の横パイプ1aとめっき
槽3の内側面との間に設置される横パイプ2aと、窒素ガ
ス配管1の縦パイプ1bのめっき槽3の内側面との間に設
置され、かつ横パイプ2aの両端を相互に連通した縦パイ
プ2bとを組合せてなるもので、空気配管2は、めっき槽
3の内底面中央部位に存在する窒素ガス配管1の外側を
取り囲むように配設されている。
The air pipe 2 is provided between a horizontal pipe 2a installed between the horizontal pipe 1a of the nitrogen gas pipe 1 and the inner surface of the plating tank 3 and an inner surface of the plating tank 3 of the vertical pipe 1b of the nitrogen gas pipe 1. The air pipe 2 surrounds the outside of the nitrogen gas pipe 1 existing at the center of the inner bottom surface of the plating tank 3. It is arranged as follows.

窒素ガス配管1と空気配管2とに用いる各パイプ1a,1
b,2a,2bは、例えば直径8mmの塩化ビニール製のものを用
い、各パイプ1a,1b,2a,2bには、窒素、空気を吹出す吹
出口が下向きに45゜の角度をもって開口してあり、めっ
き槽3の内底部での各パイプ1a,1b,2a,2bの設置間隔
は、5cmに設定してある。
Each pipe 1a, 1 used for nitrogen gas pipe 1 and air pipe 2
For b, 2a, 2b, for example, use a thing made of vinyl chloride having a diameter of 8 mm, and in each pipe 1a, 1b, 2a, 2b, an outlet for blowing nitrogen and air opens downward at an angle of 45 °. The interval between the pipes 1a, 1b, 2a, 2b at the inner bottom of the plating tank 3 is set to 5 cm.

また、溶存酸素濃度は、窒素ガス配管1の吹出口から
めっき槽3の高さ方向20cmの高さ位置で2mgdm-3、空気
配管2の吹出口からめっき槽3の高さ方向20cmの高さ位
置で5mgdm-3とする。
The dissolved oxygen concentration was 2 mgdm -3 at a height of 20 cm in the height direction of the plating tank 3 from the outlet of the nitrogen gas pipe 1, and a height of 20 cm from the outlet of the air pipe 2 in the height of the plating tank 3. 5 mgdm -3 at the position.

ここで、窒素ガス配管1から窒素ガスを、空気配管2
から空気をめっき槽3中のめっき液中に吹出すと、窒素
ガス配管1が槽内底部の中央部位に配置され、その外側
に空気配管2が配置されているため、窒素ガスと空気と
の流れが相互に規制されることとなり、第2図(a)に
示すようにめっき槽3の中央部での窒素ガス配管1の外
形四角形を底面とし、高さ方向の長方体形状の範囲で窒
素ガスが吹出され、撹拌中に溶存酸素濃度が低い領域A
が形成され、一方第2図(b)に示すように長方体形状
の溶存酸素濃度が低い領域Aの外周側でめっき槽3の内
側面との間に空気が吹出され、撹拌中に溶存酸素濃度が
比較的高い領域Bが形成される。
Here, nitrogen gas is supplied from the nitrogen gas pipe 1 to the air pipe 2
When air is blown into the plating solution in the plating tank 3 from above, the nitrogen gas pipe 1 is arranged at the center of the bottom of the tank and the air pipe 2 is arranged outside the nitrogen gas pipe 1. As shown in FIG. 2 (a), the flow is regulated mutually, and as shown in FIG. 2 (a), the outer square of the nitrogen gas pipe 1 at the center of the plating tank 3 has a bottom surface, and is within a rectangular shape in the height direction. Region A where nitrogen gas is blown out and dissolved oxygen concentration is low during stirring
On the other hand, as shown in FIG. 2 (b), air is blown out between the outer peripheral side of the rectangular shaped region A having a low dissolved oxygen concentration and the inner surface of the plating tank 3 and dissolved during stirring. A region B having a relatively high oxygen concentration is formed.

上記条件で撹拌を行ったところ、第4図に示すように
めっき槽3内の溶存酸素指数の分布は、槽端すなわち空
気配管2から空気を吹出す領域を100%とすると、槽中
央部すなわち窒素ガス配管1から窒素ガスを吹出す領域
では約40%になった。
When the stirring was performed under the above conditions, as shown in FIG. 4, the distribution of the dissolved oxygen index in the plating tank 3 was, assuming that the area at the tank end, that is, the area where air was blown out from the air pipe 2 was 100%, the tank central part, In the region where the nitrogen gas is blown out from the nitrogen gas pipe 1, the ratio becomes about 40%.

次に第2図を用いて本撹拌方法を説明する。 Next, the present stirring method will be described with reference to FIG.

窒素ガス配管1よりめっき槽3の中心部分に窒素ガス
を吹出して、めっき液の窒素ガスによる撹拌を行うとと
もに、窒素ガス配管1の外周部で空気配管2より空気を
吹出して、めっき液の空気による撹拌を行い、めっき槽
3内の溶存酸素濃度の制御を行って、めっき槽3の内側
面に接して溶存酸素高濃度領域Bを形成するとともに、
めっき槽3の中央部に溶存酸素低濃度領域Aを形成す
る。
Nitrogen gas is blown out from the nitrogen gas pipe 1 to the center of the plating tank 3 to agitate the plating solution with the nitrogen gas, and air is blown out from the air pipe 2 around the nitrogen gas pipe 1 to remove By controlling the dissolved oxygen concentration in the plating tank 3 to form a dissolved oxygen high concentration region B in contact with the inner surface of the plating tank 3,
A dissolved oxygen low concentration region A is formed in the center of the plating tank 3.

第2図(a)の領域Aは、窒素ガス配管1上の領域で
あるため、撹拌中は溶存酸素濃度を低下させ、無電解銅
めっき液を活性に保つ。第2図(b)の領域Bは、空気
配管2上の領域であるため、撹拌中は溶存酸素濃度が比
較的高く、無電解銅めっき液を第2図(a)に比べ不活
性な状態で保つ。
Since the area A in FIG. 2A is an area on the nitrogen gas pipe 1, the concentration of dissolved oxygen is reduced during stirring, and the electroless copper plating solution is kept active. Since the region B in FIG. 2B is a region on the air pipe 2, the concentration of dissolved oxygen is relatively high during stirring, and the electroless copper plating solution is inactive compared to FIG. 2A. Keep in.

以上のように本撹拌装置を用いると、一槽内に溶存酸
素濃度の異なる二つの領域を持つことができる。
As described above, by using the present stirring device, two regions having different dissolved oxygen concentrations can be provided in one tank.

本発明の撹拌方法で無電解銅めっきを行う際は、前処
理工程の後、第2図(a)に図示した溶存酸素低濃度領
域Aに治具を投入し、この領域内で揺動し、無電解銅め
っきを行う。
When performing the electroless copper plating by the stirring method of the present invention, after the pretreatment step, a jig is put into the low-concentration dissolved oxygen region A shown in FIG. And electroless copper plating.

(実施例2) 本実施例では、窒素ガス配管1と空気配管2とは、塩
化ビニル製100mmφとし、横向90゜方向に窒素ガス、空
気の吹出口を設け、槽底部の各配管の間隔は10cmとす
る。また、溶存酸素濃度は、窒素ガス配管1の吹出口か
ら20cmの高さで2.5mgdm-3、空気配管2の吹出口から同
じく20cmの高さで4mgdm-3としたものである。
(Example 2) In this example, the nitrogen gas pipe 1 and the air pipe 2 are made of 100 mmφ made of vinyl chloride, and nitrogen gas and air outlets are provided in the horizontal direction of 90 °. 10cm. Further, the dissolved oxygen concentration, nitrogen gas 2.5Mgdm -3 through the outlet of the pipe 1 at a height of 20cm, is obtained by a 4Mgdm -3 in height likewise 20cm from the air outlet of the air pipe 2.

本実施例によれば、実施例1と同様の効果を得ること
ができる。
According to this embodiment, the same effects as those of the first embodiment can be obtained.

〔発明の効果〕〔The invention's effect〕

以上説明したように本発明は、一つの槽内で窒素ガス
による溶存酸素低濃度(活性)領域と空気による溶存酸
素高濃度(不活性)領域の二つの領域を持つガス撹拌を
行うことで、次の効果がある。すなわち、 (1) 窒素ガスによる撹拌領域を持つため、建浴直
後、浴の溶存酸素濃度が飽和に達していても、これを低
下させ、浴を活性化させることができる。これにより1
回/1建浴のダミー活性を省くことができる。
As described above, the present invention performs gas agitation having two regions of a dissolved oxygen low concentration (active) region by nitrogen gas and a dissolved oxygen high concentration (inactive) region by air in one tank, It has the following effects: That is, (1) Since the bath has a stirring region by nitrogen gas, even if the dissolved oxygen concentration of the bath has reached saturation immediately after the bath is built, the concentration can be reduced and the bath can be activated. This gives 1
It is possible to omit the dummy activity of the 1st bath.

(2) 窒素ガスと空気の二つの領域を持つ撹拌を行っ
ているため、窒素ガスのみによる活性化が進み、浴が分
解することはなく、浴全体としては安定に保たれてい
る。
(2) Since the stirring is performed with the two regions of the nitrogen gas and the air, the activation with only the nitrogen gas proceeds, and the bath is not decomposed, and the bath is kept stable as a whole.

(3) 治具の投入される領域は常に活性度を保ってい
るため、ロードファクターによる投入量の調整がいらな
い。
(3) Since the area in which the jig is inserted always maintains its activity, there is no need to adjust the input amount by the load factor.

(4) 溶存酸素高濃度(不活性)領域は、槽と接して
いるため、槽への金属銅の析出はなく、めっき後の槽エ
ッチング頻度を1回/1建浴から1回/5建浴と減少でき
る。
(4) Since the dissolved oxygen high concentration (inactive) area is in contact with the tank, there is no deposition of metallic copper in the tank, and the etching frequency of the tank after plating is once / one bath to once / five times. Can be reduced with bath.

という効果を有する。It has the effect of.

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

第1図は、本発明の一実施例による無電解銅めっき浴撹
拌方法を用いためっき槽を示す斜視図、第2図(a),
(b)は、第1図の配管により槽内の撹拌を行った場合
の異なる溶存酸素濃度を持つ二つの領域を示す図、第3
図(a),(b)は、従来の撹拌方法を示す図、第4図
は、めっき槽内の溶存酸素指数を示す分布図である。 1……窒素ガス配管、2……空気配管 3……めっき槽 A……溶存酸素低濃度領域 B……溶存酸素高濃度領域
FIG. 1 is a perspective view showing a plating tank using an electroless copper plating bath stirring method according to one embodiment of the present invention.
(B) is a diagram showing two regions having different dissolved oxygen concentrations when the inside of the tank is agitated by the piping of FIG.
FIGS. (A) and (b) are diagrams showing a conventional stirring method, and FIG. 4 is a distribution diagram showing a dissolved oxygen index in a plating tank. 1 ... Nitrogen gas piping, 2 ... Air piping 3 ... Plating tank A ... Dissolved oxygen low concentration region B ... Dissolved oxygen high concentration region

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C23C 18/16 - 18/52 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 7 , DB name) C23C 18/16-18/52

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ガス吹出工程と、濃度制御工程とを有し、
めっき槽内のめっき液を攪拌する無電解銅めっき浴攪拌
方法であって、 前記ガス吹出工程は、一つのめっき槽内の内底面中央部
に配設された窒素ガス配管とこの外周を取り囲むように
配設された空気配管とのそれぞれの上方の領域内に、窒
素ガス配管から窒素ガスを、空気配管から空気を吹出し
て、窒素ガスと空気とを併用してめっき液のガス攪拌を
行う工程であり、 前記濃度制御工程は、前記窒素ガス配管と前記空気配管
とのそれぞれの上方の領域内に対応して、めっき槽内の
中央部に窒素ガスによる溶存酸素低濃度領域とめっき槽
の内側面に接して空気による溶存酸素高濃度領域との異
なる二つの領域を一つのめっき槽内に形成する工程であ
ることを特徴とする無電解銅めっき浴攪拌方法。
1. A method according to claim 1, further comprising a gas blowing step and a concentration controlling step.
A method of stirring an electroless copper plating bath for stirring a plating solution in a plating tank, wherein the gas blowing step surrounds a nitrogen gas pipe disposed in a central portion of an inner bottom surface in one plating tank and an outer periphery thereof. A step of blowing nitrogen gas from a nitrogen gas pipe and air from an air pipe into a region above each of the air pipes disposed in the gas pipe and performing gas agitation of the plating solution using the nitrogen gas and the air together. The concentration control step corresponds to a region above each of the nitrogen gas pipe and the air pipe, and a dissolved oxygen low-concentration region due to nitrogen gas in a central portion of the plating tank and the plating tank. A method for agitating an electroless copper plating bath, comprising a step of forming two regions in contact with a side surface, which are different from a region of high concentration of dissolved oxygen due to air, in one plating tank.
JP2281342A 1990-10-19 1990-10-19 Electroless copper plating bath stirring method Expired - Lifetime JP3038876B2 (en)

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JP2281342A JP3038876B2 (en) 1990-10-19 1990-10-19 Electroless copper plating bath stirring method

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Application Number Priority Date Filing Date Title
JP2281342A JP3038876B2 (en) 1990-10-19 1990-10-19 Electroless copper plating bath stirring method

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JPH04157170A JPH04157170A (en) 1992-05-29
JP3038876B2 true JP3038876B2 (en) 2000-05-08

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8441037B2 (en) 2009-03-31 2013-05-14 Asahi Kasei Microdevices Corporation Semiconductor device having a thin film stacked structure

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8441037B2 (en) 2009-03-31 2013-05-14 Asahi Kasei Microdevices Corporation Semiconductor device having a thin film stacked structure

Also Published As

Publication number Publication date
JPH04157170A (en) 1992-05-29

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