JP2010138429A - Electrolytic copper plating method using insoluble anode - Google Patents

Electrolytic copper plating method using insoluble anode Download PDF

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JP2010138429A
JP2010138429A JP2008313667A JP2008313667A JP2010138429A JP 2010138429 A JP2010138429 A JP 2010138429A JP 2008313667 A JP2008313667 A JP 2008313667A JP 2008313667 A JP2008313667 A JP 2008313667A JP 2010138429 A JP2010138429 A JP 2010138429A
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copper plating
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Kazue Ban
和恵 伴
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Shinko Electric Industries Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To solve the problem that, in a conventional electrolytic copper plating method using an insoluble anode, it is difficult to suppress an rapid increase of the dissolved oxygen concentration in an electrolytic copper plating solution caused by supplying copper oxide (II) as a copper source. <P>SOLUTION: When electrolytic copper plating using an insoluble anode is applied to an object to be plated immersed in an electrolytic copper plating solution into which copper sulfate is added, copper oxide is replenished as a copper source to the electrolytic copper plating solution, and at that time, iron (II) sulfate is added to the electrolytic copper plating solution in order to suppress the dissolved oxygen concentration in the electrolytic copper plating solution, that increases by the supply of copper oxide (II). <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は不溶性陽極を用いた電解銅めっき方法に関し、更に詳細には硫酸銅が添加された電解銅めっき液に浸漬しためっき対象に、不溶性陽極を用いて電解銅めっきを施す不溶性陽極を用いた電解銅めっき方法に関する。   The present invention relates to an electrolytic copper plating method using an insoluble anode, and more specifically, an insoluble anode in which electrolytic copper plating is performed using an insoluble anode on a plating object immersed in an electrolytic copper plating solution to which copper sulfate is added. The present invention relates to an electrolytic copper plating method.

硫酸銅が添加された電解銅めっき液を用いた電解銅めっきは、配線基板の配線パターンの形成等に広く採用されている。
従来、かかる電解銅めっきでは、陽極に溶解性陽極が用いられていたが、めっき液管理等が容易な不溶解性陽極を用いることも増加してきている。
かかる不溶解性陽極を用いた電解銅めっきでは、溶解性陽極が溶解することに因る銅の補給がないため、電解銅めっき液中の銅濃度が減少してくる。このため、電解銅めっき液に酸化銅(II)等の銅成分を補給することが必要である。
Electrolytic copper plating using an electrolytic copper plating solution to which copper sulfate is added has been widely adopted for the formation of wiring patterns on wiring boards.
Conventionally, in such electrolytic copper plating, a soluble anode has been used as the anode, but the use of an insoluble anode that facilitates plating solution management and the like has also increased.
In electrolytic copper plating using such an insoluble anode, there is no replenishment of copper due to dissolution of the soluble anode, so the copper concentration in the electrolytic copper plating solution decreases. Therefore, it is necessary to replenish the electrolytic copper plating solution with a copper component such as copper (II) oxide.

ところで、不溶解性陽極を用いた電解銅めっきでは、電極反応によって陽極で発生した酸素が電解銅めっき液中に溶け込むことによって溶存酸素が増加する。かかる溶存酸素が電解銅めっき液中で増加すると、電解銅めっき液中に添加した添加物が酸化される等の悪影響がある。
このため、下記特許文献1では、電解銅めっき液を空気攪拌又は不活性ガスによる攪拌によって、電解銅めっき液中の溶存酸素濃度を30mg/L以下に維持する電解銅めっき方法が提案されている。
特開2007−169700号公報
By the way, in electrolytic copper plating using an insoluble anode, dissolved oxygen increases as oxygen generated at the anode by electrode reaction dissolves in the electrolytic copper plating solution. When such dissolved oxygen increases in the electrolytic copper plating solution, there are adverse effects such as oxidation of additives added to the electrolytic copper plating solution.
For this reason, the following Patent Document 1 proposes an electrolytic copper plating method for maintaining the dissolved oxygen concentration in the electrolytic copper plating solution at 30 mg / L or less by stirring the electrolytic copper plating solution with air or stirring with an inert gas. .
JP 2007-169700 A

前掲の特許文献1で提案された電解銅めっき方法によれば、電解銅めっき中に発生する酸素に起因する電解銅めっき液中の溶存酸素濃度の増加を抑制できる。
しかしながら、本発明者の検討によれば、電解銅めっき液に銅源として酸化銅(II)を補給した際にも、電解銅めっき液中の溶存酸素濃度が増加することが判明した。かかる酸化銅(II)の補給に因る電解銅めっき液中の溶存酸素の増加は急激であって、通常の電解銅めっき液の攪拌程度では到底抑制できず、電解銅めっき液中の溶存酸素濃度が高い状態が継続する。このため、電解銅めっき液中に添加されている光沢剤等の添加剤の酸化が進行し、電解銅めっき液中の添加剤のバランスが崩れ、めっき不良が発生するおそれがある。
そこで、本発明は、電解銅めっき液に銅源としての酸化銅(II)を補給することによって発生した電解銅めっき液中の溶存酸素濃度が急増する状態を抑制困難な従来の不溶性陽極を用いた電解銅めっき方法の課題を解消し、電解銅めっき液に銅源としての酸化銅(II)を補給した際に、電解銅めっき液中の溶存酸素濃度が急増する状態を抑制できる不溶性陽極を用いた電解銅めっき方法を提供することにある。
According to the electrolytic copper plating method proposed in the aforementioned Patent Document 1, it is possible to suppress an increase in dissolved oxygen concentration in the electrolytic copper plating solution due to oxygen generated during electrolytic copper plating.
However, according to the study by the present inventor, it has been found that the dissolved oxygen concentration in the electrolytic copper plating solution also increases when copper (II) oxide is supplied to the electrolytic copper plating solution as a copper source. The increase in dissolved oxygen in the electrolytic copper plating solution due to the replenishment of copper (II) oxide is abrupt, and it cannot be completely suppressed by stirring the ordinary electrolytic copper plating solution, and dissolved oxygen in the electrolytic copper plating solution. High concentration continues. For this reason, the oxidation of additives such as brighteners added in the electrolytic copper plating solution proceeds, the balance of the additives in the electrolytic copper plating solution is lost, and plating failure may occur.
Therefore, the present invention uses a conventional insoluble anode in which it is difficult to suppress the state where the dissolved oxygen concentration in the electrolytic copper plating solution generated by replenishing the electrolytic copper plating solution with copper (II) oxide as a copper source is rapidly increased. An insoluble anode that can suppress the state of rapidly increasing the dissolved oxygen concentration in the electrolytic copper plating solution when the electrolytic copper plating solution is solved and copper (II) oxide as the copper source is replenished to the electrolytic copper plating solution It is in providing the used electrolytic copper plating method.

本発明者は、前記課題を解決すべく検討を重ねた結果、不溶性陽極を用いた電解銅めっき液に、銅源としての酸化銅(II)を補給すると共に、硫酸鉄を添加したところ、電解銅めっき液中の溶存酸素濃度の急激な増加を抑制できることを見出し、本発明に到達した。
すなわち、本発明は、硫酸銅が添加された電解銅めっき液に浸漬しためっき対象に、不溶性陽極を用いて電解銅めっきを施す際に、前記電解銅めっき液に対して銅源として酸化銅を補給し、その際に、前記酸化銅の補給によって電解銅めっき液中に増加する溶存酸素濃度を抑制すべく、前記電解銅めっき液に周期律表の第VIII族の鉄族元素に属する金属元素を前記電解銅めっき液に添加することを特徴とする不溶性陽極を用いた電解銅めっき方法にある。
かかる本発明において、電解銅めっき液に添加する金属元素を、硫酸塩又はその水和物、亜硫酸塩又は塩化物塩として電解銅めっき液に添加することによって、電解銅めっき液中に鉄族元素に属する金属元素のイオンを存在させることができる。
この電解銅めっき液に添加する金属元素としては、鉄、ニッケル又はコバルトを好適に用いることができる。
As a result of repeated investigations to solve the above problems, the present inventor replenished electrolytic copper plating solution using an insoluble anode with copper (II) oxide as a copper source and added iron sulfate. The present inventors have found that a rapid increase in the dissolved oxygen concentration in the copper plating solution can be suppressed, and have reached the present invention.
That is, in the present invention, when subjecting a plating object immersed in an electrolytic copper plating solution added with copper sulfate to electrolytic copper plating using an insoluble anode, copper oxide is used as a copper source for the electrolytic copper plating solution. In order to suppress the dissolved oxygen concentration that increases in the electrolytic copper plating solution due to the replenishment of the copper oxide, a metal element belonging to the group VIII iron group element of the periodic table is added to the electrolytic copper plating solution. Is added to the electrolytic copper plating solution in the electrolytic copper plating method using an insoluble anode.
In the present invention, by adding a metal element added to the electrolytic copper plating solution to the electrolytic copper plating solution as a sulfate or a hydrate thereof, a sulfite or a chloride salt, an iron group element is contained in the electrolytic copper plating solution. Metal element ions belonging to can be present.
As the metal element added to the electrolytic copper plating solution, iron, nickel, or cobalt can be suitably used.

本発明に係る不溶解性陽極を用いた電解銅めっき方法によれば、硫酸銅が添加された電解銅めっき液に銅源として酸化銅(II)を補給する際に、溶存酸素濃度の急激な増加を抑制、或いは溶存酸素濃度が増加しても迅速に低下でき、添加剤の分解を抑制できる。
その結果、電解銅めっき液中に添加されている光沢剤等の添加剤の酸化が進行することに起因して、電解銅めっき液中の添加剤のバランスが崩れて、めっき不良が発生するおそれを解消できる。
According to the electrolytic copper plating method using the insoluble anode according to the present invention, when copper (II) oxide is replenished as a copper source to the electrolytic copper plating solution to which copper sulfate is added, the dissolved oxygen concentration is rapidly increased. Even if the increase is suppressed or the dissolved oxygen concentration is increased, it can be rapidly decreased and decomposition of the additive can be suppressed.
As a result, the oxidation of additives such as brighteners added in the electrolytic copper plating solution proceeds, and the balance of the additives in the electrolytic copper plating solution may be lost, resulting in poor plating. Can be eliminated.

本発明で用いる電解銅めっき液としては、例えば下記表1に示す組成の電解銅めっき液を上げることができる。   As an electrolytic copper plating solution used in the present invention, for example, an electrolytic copper plating solution having a composition shown in Table 1 below can be raised.

Figure 2010138429
その他添加剤としては、電析作用を促進するブライトナー、凸部の電析作用を抑制するレベラー、非イオン界面活性剤からなるポリマー等を上げることができる。
かかる電解銅めっき液に、銅源の補給として酸化銅(II)のみを添加すると、下記化1に示す様に、CuOは電解銅めっき液中の遊離硫酸と反応し、硫酸銅と水になる。
Figure 2010138429
Figure 2010138429
Examples of other additives include a brightener that promotes the electrodeposition effect, a leveler that suppresses the electrodeposition effect of the convex portion, and a polymer composed of a nonionic surfactant.
When only copper (II) oxide is added to the electrolytic copper plating solution as a copper source, CuO reacts with free sulfuric acid in the electrolytic copper plating solution to form copper sulfate and water, as shown in the following chemical formula 1. .
Figure 2010138429

かかる酸化銅(II)の溶解反応時に、電解銅めっき液中の溶存酸素濃度が急激に上昇し、電解銅めっき液中の光沢剤等の添加剤成分が酸化され、本来の機能を失う。このため、電解銅めっき液中の添加剤のバランスが崩れめっき工程に不具合が生じるおそれがある。   During the dissolution reaction of copper (II) oxide, the concentration of dissolved oxygen in the electrolytic copper plating solution increases rapidly, and additive components such as brighteners in the electrolytic copper plating solution are oxidized and lose their original function. For this reason, the balance of the additive in the electrolytic copper plating solution may be lost, and there may be a problem in the plating process.

この点、本発明では、電解銅めっき液に、銅源の補給として酸化銅(II)を添加する前後に、周期律表の第VIII族の鉄族元素に属する金属元素を添加することによって、酸化銅(II)の溶解反応時に、電解銅めっき液中の溶存酸素濃度の急激な増加を抑制、或いは溶存酸素濃度が増加しても迅速に低下することができる。このため、電解銅めっき液中の添加剤の酸化分解を抑制でき、電解銅めっき液中の添加剤のバランスを維持できる。
この様に、酸化銅(II)を添加する前後に、周期律表の第VIII族の鉄族元素に属する金属元素を添加することによって、電解銅めっき液中の溶存酸素濃度の急激な増加を抑制等できるのは、電解銅めっき液中の周期律表の第VIII族の鉄族元素に属する金属元素のイオンが、電解銅めっき液中の溶存酸素と反応することによると考えられる。
In this regard, in the present invention, before and after adding copper (II) oxide as a copper source supplement to the electrolytic copper plating solution, by adding a metal element belonging to the Group VIII iron group element of the periodic table, During the dissolution reaction of copper (II) oxide, a rapid increase in the dissolved oxygen concentration in the electrolytic copper plating solution can be suppressed, or even if the dissolved oxygen concentration is increased, it can be rapidly lowered. For this reason, the oxidative decomposition of the additive in the electrolytic copper plating solution can be suppressed, and the balance of the additive in the electrolytic copper plating solution can be maintained.
Thus, before and after adding copper oxide (II), by adding a metal element belonging to the group VIII iron group element of the periodic table, the concentration of dissolved oxygen in the electrolytic copper plating solution is rapidly increased. The suppression can be attributed to the fact that ions of metal elements belonging to Group VIII iron group elements of the periodic table in the electrolytic copper plating solution react with dissolved oxygen in the electrolytic copper plating solution.

かかる周期律表の第VIII族の鉄族元素に属する金属元素としては、鉄、ニッケル又はコバルトを好適に用いることができる。特に、鉄を好適に用いることができる。
また、電解銅めっき液に添加する金属元素としては、電解銅めっき液中で容易にイオン化する形態で添加することが好ましい。かかる形態としては、硫酸塩又はその水和物、亜硫酸塩又は塩化物塩を上げることができる。
周期律表の第VIII族の鉄族元素に属する金属元素は、酸化銅(II)の添加と同時に添加することが好ましいが、酸化銅(II)の添加前5分〜酸化銅(II)の添加後5分までの期間内に添加することができる。
また、かかる金属元素の添加量は、0.05mol%以上、好ましくは0.01〜10.0mol%程度とすることが好ましい。
尚、周期律表の第VIII族の鉄族元素に属する金属元素を電解銅めっき液に添加しても、添加した金属元素がめっき対象に析出したり、或いは陽極に析出する等の悪影響は見られない。
As the metal element belonging to the Group VIII iron group element of the periodic table, iron, nickel or cobalt can be preferably used. In particular, iron can be preferably used.
Moreover, it is preferable to add as a metal element added to an electrolytic copper plating solution in the form which ionizes easily in an electrolytic copper plating solution. As such a form, sulfate or its hydrate, sulfite, or chloride salt can be raised.
The metal element belonging to the Group VIII iron group element of the periodic table is preferably added simultaneously with the addition of copper (II) oxide, but from 5 minutes before the addition of copper (II) oxide to copper (II) oxide. It can be added within a period of up to 5 minutes after addition.
The amount of the metal element added is 0.05 mol% or more, preferably about 0.01 to 10.0 mol%.
Even if a metal element belonging to the Group VIII iron group element of the periodic table is added to the electrolytic copper plating solution, there is an adverse effect such that the added metal element is deposited on the plating object or deposited on the anode. I can't.

硫酸銅を添加した電解銅めっき液の代わりに、1.2mol/Lの硫酸水溶液を調整した。この硫酸水溶液中の溶存酸素を測定したところ、約7.5mg/Lの溶存酸素が検出された。
次いで、硫酸水溶液に0.006molの硫酸鉄(II)・7水和物を添加した後、0.1molの酸化銅(II)を添加して、溶存酸素濃度の経時変化を測定した。その結果を図1に示す。
図1から明らかな様に、酸化銅(II)の溶解時に発生する溶存酸素濃度の上昇を抑制できる。
Instead of the electrolytic copper plating solution to which copper sulfate was added, a 1.2 mol / L sulfuric acid aqueous solution was prepared. When dissolved oxygen in this sulfuric acid aqueous solution was measured, about 7.5 mg / L of dissolved oxygen was detected.
Next, 0.006 mol of iron (II) sulfate heptahydrate was added to the sulfuric acid aqueous solution, and then 0.1 mol of copper (II) oxide was added, and the change over time in the dissolved oxygen concentration was measured. The result is shown in FIG.
As is apparent from FIG. 1, it is possible to suppress an increase in dissolved oxygen concentration that occurs when copper (II) oxide is dissolved.

実施例1において、硫酸鉄(II)・7水和物に代えて、硫酸コバルト(II)・7水和物を用いた他は、実施例1と同様にして、0.1molの酸化銅(II)を添加して、溶存酸素濃度の経時変化を測定した。その結果を図2に示す。
図2から明らかな様に、酸化銅(II)の溶解時に溶存酸素濃度が上昇するものの、迅速に溶存酸素濃度が低下する。
In Example 1, in place of iron (II) sulfate heptahydrate, cobalt mol (II) sulfate heptahydrate was used in the same manner as in Example 1, except that 0.1 mol of copper oxide ( II) was added and the time course of dissolved oxygen concentration was measured. The result is shown in FIG.
As is apparent from FIG. 2, the dissolved oxygen concentration increases rapidly when copper (II) oxide is dissolved, but the dissolved oxygen concentration rapidly decreases.

比較例Comparative example

実施例1において、硫酸鉄(II)・7水和物を添加することなく、0.1molの酸化銅(II)を添加して、溶存酸素濃度の経時変化を測定した。その結果を図3に示す。
図3から明らかな様に、酸化銅(II)の溶解時に溶存酸素濃度が急激に増加し、且つ溶存酸素濃度が増加した状態が暫く維持される。
In Example 1, 0.1 mol of copper (II) oxide was added without adding iron (II) sulfate heptahydrate, and the change with time in the dissolved oxygen concentration was measured. The result is shown in FIG.
As is apparent from FIG. 3, the dissolved oxygen concentration rapidly increases when the copper (II) oxide is dissolved, and the state where the dissolved oxygen concentration is increased is maintained for a while.

実施例1の溶存酸素濃度の経時変化を示すグラフである。2 is a graph showing the change with time of the dissolved oxygen concentration in Example 1. FIG. 実施例2の溶存酸素濃度の経時変化を示すグラフである。6 is a graph showing the change with time of the dissolved oxygen concentration in Example 2. 比較例の溶存酸素濃度の経時変化を示すグラフである。It is a graph which shows a time-dependent change of the dissolved oxygen concentration of a comparative example.

Claims (3)

硫酸銅が添加された電解銅めっき液に浸漬しためっき対象に、不溶性陽極を用いて電解銅めっきを施す際に、
前記電解銅めっき液に対して銅源として酸化銅を補給し、その際に、前記酸化銅の補給によって電解銅めっき液中に増加する溶存酸素濃度を抑制すべく、前記電解銅めっき液に周期律表の第VIII族の鉄族元素に属する金属元素を前記電解銅めっき液に添加することを特徴とする不溶性陽極を用いた電解銅めっき方法。
When applying electrolytic copper plating to an object to be plated immersed in an electrolytic copper plating solution to which copper sulfate has been added using an insoluble anode,
Copper oxide is replenished as a copper source to the electrolytic copper plating solution, and at that time, in order to suppress the dissolved oxygen concentration that increases in the electrolytic copper plating solution by replenishing the copper oxide, the electrolytic copper plating solution is cycled. An electrolytic copper plating method using an insoluble anode, characterized in that a metal element belonging to the group VIII iron group element of the table is added to the electrolytic copper plating solution.
電解銅めっき液に添加する金属元素を、硫酸塩又はその水和物、亜硫酸塩又は塩化物塩として電解銅めっき液に添加する請求項1記載の不溶性陽極を用いた電解銅めっき方法。   The electrolytic copper plating method using the insoluble anode according to claim 1, wherein the metal element added to the electrolytic copper plating solution is added to the electrolytic copper plating solution as a sulfate or a hydrate thereof, a sulfite or a chloride salt. 電解銅めっき液に添加する金属元素として、鉄、ニッケル又はコバルトを用いる請求項1又は請求項2記載の不溶性陽極を用いた電解銅めっき方法。   The electrolytic copper plating method using the insoluble anode according to claim 1 or 2, wherein iron, nickel, or cobalt is used as a metal element added to the electrolytic copper plating solution.
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JP2014111811A (en) * 2012-12-05 2014-06-19 Sumitomo Metal Mining Co Ltd Copper plating method

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