WO2002046492A1 - Process for producing plating solution for electroless platinum plating, plating solution for electroless platinum plating, and method of electroless platinum plating - Google Patents

Process for producing plating solution for electroless platinum plating, plating solution for electroless platinum plating, and method of electroless platinum plating Download PDF

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Publication number
WO2002046492A1
WO2002046492A1 PCT/JP2001/010608 JP0110608W WO0246492A1 WO 2002046492 A1 WO2002046492 A1 WO 2002046492A1 JP 0110608 W JP0110608 W JP 0110608W WO 0246492 A1 WO0246492 A1 WO 0246492A1
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plating
electroless platinum
complex
solution
platinum plating
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PCT/JP2001/010608
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French (fr)
Japanese (ja)
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Katsutsugu Kitada
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Tanaka Kikinzoku Kogyo K.K.
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31Coating with metals
    • C23C18/42Coating with noble metals
    • C23C18/44Coating with noble metals using reducing agents

Definitions

  • the present invention relates to an electroless plating solution having excellent stability and capable of producing a high-quality platinum thin film.
  • the present invention also relates to a method for plating platinum using the electroless platinum plating solution.
  • this electroless platinum plating solution has a certain effect due to its stabilizer
  • the plating solution containing such a stabilizer has the problem that decomposition occurs when the plating solution is replenished during the plating operation. There is. Therefore, the plating operation using this plating solution is based on a batch process, which is not suitable for a continuous plating operation, but this does not allow efficient plating.
  • electroless platinum plating described in JP-A-5-222543.
  • the plating solution is mainly composed of a tetravalent platinum amine salt represented by the general formula [Pt (NH 3 ) 6 X], and is used for continuous plating without a stabilizer. It is disclosed that platinum plating can be performed stably. According to this plating liquid, it is possible to produce a high-quality platinum thin film, and it is also applicable to the plating of decorative articles because of its good gloss.
  • the stability of the electroless platinum plating solution described in Japanese Patent Application Laid-Open No. 5-222543 is not always sufficient, and the present inventor conducted preliminary tests.
  • the present invention has been made in view of the above background, and has extremely high stability, enables continuous plating operation, and has an electroless platinum plating solution capable of producing a high-quality thin film.
  • the purpose is to provide. And it aims at providing the plating method using this plating solution. Disclosure of the invention
  • the present inventor evaluated the stability of the electroless platinum plating solution containing the above hexaminoplatinum complex ([Pt (NH 3 ) 6 X]) as a main component, After a detailed study to improve the stability, it was found that this plating solution contained the following impurities, although it contained a tetravalent hexaaminoplatinum complex as a main component. Equation 1
  • Such impurities are considered to be generated in the process of preparing the plating solution during the production of the hexaminoaminoplatinum complex salt used as the raw material, but are less stable than the hexaminoplatinum complex as the main component. It decomposes in the solution to produce platinum fine particles that easily adhere to the plating tank wall and the adherend. Then, the catalytic action of the platinum fine particles promotes the deposition of platinum on portions other than the plating tank wall surface and the plated portion of the adherend.
  • the present inventor has determined that in order to improve the stability of the plating solution, it is necessary to eliminate the above-mentioned impurities, and for that purpose, in the production process of the plating solution, a hexaminoplatinum complex was used. It was considered appropriate to purify in advance.
  • a hexaneaminoplatinum complex salt as a raw material is made into an aqueous solution, and carbon dioxide gas is blown into the aqueous solution. A technique for extracting platinum complexes was found.
  • the reason for once reacting with the carbon dioxide gas is that the carbonate ions have excellent reactivity and selectivity with respect to the tetravalent hexaminoaminoplatinum complex to be purified.
  • This is based on the idea that the hexaminoaminoplatinum complex can be extracted with high purity. That is, the present invention provides a method for producing an electroless platinum plating solution containing a hexaminoplatinum complex using a salt of the hexaminoplatinum complex represented by the following general formula as a raw material, A method for producing an electroless platinum plating solution, which comprises a step of purifying a complex. Equation 2
  • a is, C n H 2 n + 1 NH 2 (n is an amino group represented by 0 to 1 0 integer).
  • a hexaminoplatinum complex salt is converted into an aqueous solution.
  • a hydroxide as the hexamino platinum complex salt. This is because coprecipitation of impurities is the least in the subsequent step of reacting with carbon dioxide to form carbonate.
  • the amount of the hexaaminoplatinum complex salt dissolved in the aqueous solution is preferably 1 g / L to 20 gZL in terms of platinum.
  • the amount is less than 1 gZL, a sufficient amount of carbonate cannot be purified, and the efficiency is low. Also, if it exceeds 20 gZL, the salt will not be dissolved. Then, carbon dioxide gas is blown into the aqueous solution to precipitate carbonates.
  • the amount of carbon dioxide gas passing here depends on the concentration of the hexaminoplatinum complex salt solution in the aqueous solution. As a guide, it is better to blow carbon dioxide gas until the solution becomes neutral.
  • the hexaminoaminoplatinum complex in the aqueous solution precipitates as a carbonate.
  • This carbonate is a high purity hexaaminoplatinum complex carbonate that does not contain the above-mentioned impurities.
  • the carbonate is dissolved with an acid in order to extract the hexaminoplatinum complex for platinum plating from the carbonate.
  • an acid for dissolving the carbonate a halogen acid such as hydrochloric acid can also dissolve the carbonate.
  • the halogen remains in the dissolution solution, and this is fixed.
  • the thin film is adsorbed on the thin film, thereby decreasing the deposition rate and darkening the appearance of the thin film.
  • sulfuric acid generates sulfate, and nitric acid has a problem that the appearance of the thin film is deteriorated.
  • an organic sulfonic acid such as methanesulfonic acid or ethanesulfonic acid
  • a low molecular weight organic carboxylic acid such as acetic acid or propionic acid.
  • These acids are added in the form of an aqueous solution.
  • carbonate ions remain in the solution after the addition of the acid, it is desirable to remove the carbonate ions when producing the plating solution.
  • co 2 a carbonate in which dissolve in an acid such as an organic sulfonic acid or organic carboxylic acids described above can be foamed easily carbonate by to Rukoto reduced pressure atmosphere solution upon dissolution The ions are removed.
  • the aqueous solution after these purification steps is a high-purity hexaaminoplatinum complex solution.
  • the hexaminoplatinum complex solution can be used as it is as an electroless platinum plating solution, but it may be appropriately diluted to bring the concentration of the platinum complex to a predetermined concentration. It can be a platinum plating liquid.
  • a reducing agent As this reducing agent, phosphinic acid, phosphonic acid, hydrazine, boron hydride, formalin, L-ascorbic acid, formic acid and the like are applicable.
  • concentration of these reducing agents is preferably 1 to 10 times the platinum ion concentration (molar concentration) in the plating solution.
  • the plating solution according to the present invention enables the production of a high-precision thin film.
  • a leveling agent may be applied to a general electroless plating solution other than platinum.
  • a cationic surfactant is applied.
  • the platinum thin film intended for the production of the present invention tends to adsorb the organic substances in these surfactants, so that the deposition rate is reduced and, in some cases, the deposition reaction is interrupted. When these surfactants are added, insoluble precipitates may be formed.
  • the leveling agent for the electroless plating solution of the present invention polyoxyethylene alkyl ether, polyalkylphenyl ether, polyoxyethylene polyoxypropyl alkyl ether, dalyserine ester, polyglycerin ester, sorbitan ester It is preferable to use a nonionic surfactant such as ester.
  • the concentration of these leveling agents is preferably 0.1 to 100 ppm.
  • the conditions for performing platinum plating using the electroless platinum plating solution according to the present invention are as follows: pH is set to 8 to 12, and the liquid temperature is set to 40 to 80 ° C. It is good. This is because, when the pH is less than pH 8, precipitation of platinum does not occur, and when the pH exceeds pH 12, the working environment deteriorates. In addition, when the liquid temperature is lower than 40 ° C, platinum does not precipitate, and when the liquid temperature is higher than 80 ° C, evaporation of amine in the plating liquid becomes remarkable.
  • pH of this plating solution add acid or aluminum to the plating solution.
  • adding the alkali it is necessary to apply an alkali having the same amino group as the amino group (a in Chemical formula 3) coordinated to platinum in the hexamino platinum complex. Is preferred.
  • First Embodiment 5 L of a “Pt (NH 3 ) 6 ] (OH) 4 solution having a platinum concentration of 10 gZL was prepared, and carbon dioxide gas was blown into the solution for 3 hours. The carbonate was weighed so that the amount of platinum contained was 30 g, and 45 mL of acetic acid was added thereto to dissolve the carbonate, and further water was added. Then, the solution after dissolution was reduced in pressure to remove carbonic acid.
  • Kisaamino platinum complex solution to the purified [P t (NH 3) 6] (CH 3 COO) 4 solution) was taken platinum amount 3 g portion of the solution (1 0 OML), reduced to this
  • glycerin ester (20 ppm) was further added as a leveling agent.
  • the electroless platinum plating solution produced as described above was heated to a temperature of 60 ° C., and an alumina plate treated with a catalyst was immersed in the solution to perform platinum plating. As a result, platinum with good gloss was deposited at a deposition rate of 1: 8 mZh.
  • the plating solution after the plating treatment was left for one week, but it was confirmed that the plating solution did not decompose.
  • Second Embodiment: [P t (NH 3) 6] in 1 0 GZL platinum concentration (OH) 4 was prepared, and carbon dioxide gas was blown into the solution for 3 hours. The precipitated carbonate was collected by filtration, washed, and dried. Next, 50 mL of maleic sulfonic acid was added to the carbonate to dissolve the carbonate, and water was further added to make the volume 1 L, and then the carbonic acid was removed from the solution.
  • a solution (100 mL) of 3 g of platinum was collected from the platinum complex solution, and 3 mL of hydrazine monohydrate was added as a reducing agent to adjust the solution pH to pH 10.5.
  • deionized water was added so as to have a liquid volume of 1 L, and polyoxyethylene dodecyl ether 20 ppm as a leveling agent was further added.
  • a platinum plating treatment was performed on an alumina plate at a liquid temperature of 60 ° C. As a result, platinum with good gloss was deposited at a deposition rate of 1.3 zm / h.
  • a carbonate is produced using an aqueous solution of [Pt (NH 3 ) 6 ] (OH) 4 as a raw material.
  • 6 OmL of ethanesulfonic acid was added to dissolve the carbonate, and a reducing agent was added to adjust the pH and the volume of the solution to produce a plating solution.
  • other conditions such as the concentration of [Pt (NH 3 ) 6 ] (OH) 4 are the same as in the second embodiment.
  • the plating rate was 2.0 m_ / h, which was not inferior to those of the first to fifth embodiments. Deposition speed was obtained, but when the plating solution after the plating treatment was allowed to stand, platinum was deposited on the bottom and wall of the plating tank one day later. Was confirmed. This is because, although the stabilizer was added in the comparative example, the raw material [Pt (NH 3 ) 6 ] (OH) 4 was not purified, and the impurities contained therein caused the purification. It is considered that the plating liquid was decomposed. Industrial applicability
  • the present invention aims to further improve the stability of a conventional electroless platinum plating solution containing a hexaminoaminoplatinum complex as a main component, and to improve the stability of an electroless platinum plating solution for purifying a hexaminoplatinum complex.
  • This is a method of producing an electroless platinum plating solution, which does not contain impurities and does not decompose the composition of the solution during the plating operation.
  • a high-quality platinum thin film can be produced from its stability.

Abstract

A process for producing from a hexaaminoplatinum complex salt a plating solution for electroless platinum plating which contains the hexaaminoplatinum complex, characterized by including a process for hexaaminoplatinum complex purification which comprises (a) a step in which an aqueous solution of a hexaaminoplatinum complex salt as a starting material is prepared and carbon dioxide is passed through the aqueous solution to produce the carbonate of the hexaaminoplatinum complex and (b) a step in which the hexaaminoplatinum complex carbonate is dissolved with an acid.

Description

明細書  Specification
無電解白金めつき液の製造方法及び無電解白金めつき液並びに無電解 白金めつき方法 技術分野 Method for producing electroless platinum plating liquid, electroless platinum plating liquid and electroless platinum plating method
本発明は、 安定性に優れ、 高品質の白金薄膜を製造可能な無電解白 金めつき液に関する。 また、 この無電解白金めつき液を用いた白金め つき方法に関する。 背景技術  TECHNICAL FIELD The present invention relates to an electroless plating solution having excellent stability and capable of producing a high-quality platinum thin film. The present invention also relates to a method for plating platinum using the electroless platinum plating solution. Background art
無電解白金めつき液としては、 これまでいくつかのものが知られて いるが、 それらの多くには安定性に関する問題があり十分な実用化へ の可能性を有していない。 また、 この安定性の問題に対する解決策を 提示しつつも十分なものを開示したものも少ない。 例えば、 特公昭 5 9 - 3 3 6 6 7号公報では、 白金イオンとしてニトロ錯体又は二卜口 アンミン錯体を含み、 還元剤としてヒドラジンを、 そして、 安定化剤 としてヒドロキシルアミン塩を添加した無電解白金めつき液が開示さ れている。 この無電解白金めつき液は、 ヒドラジンが優れた還元作用 を有しつつも、 液組成の安定性を低下させるという不利益に着目し、 その安定性の改善策として安定化剤としてヒドロキシルアミン塩を選 択添加したものである。  Several electroless platinum plating solutions have been known so far, but many of them have problems with stability and do not have sufficient potential for practical use. In addition, few provide solutions to this stability problem but disclose enough. For example, Japanese Patent Publication No. Sho 59-33667 discloses an electroless method in which a nitro complex or a nitroamine ammine complex is contained as a platinum ion, hydrazine is added as a reducing agent, and a hydroxylamine salt is added as a stabilizer. A platinum plating liquid is disclosed. This electroless platinum plating solution focuses on the disadvantage of reducing the stability of the liquid composition while hydrazine has an excellent reducing action, and as a measure to improve the stability, hydroxylamine salt is used as a stabilizer. Was selectively added.
この無電解白金めつき液はその安定化剤による一応の効果は認めら れるものの、 このような安定化剤を含有するめつき液では、 めっき操 業中にめっき液を補充すると分解が生じるという問題がある。従って、 このめつき液を適用しためつき操業は、バッチ処理を基本としており、 連続的なめっき操業に対しては不向きであるが、 これでは効率的なめ つき処理はできない。  Although this electroless platinum plating solution has a certain effect due to its stabilizer, the plating solution containing such a stabilizer has the problem that decomposition occurs when the plating solution is replenished during the plating operation. There is. Therefore, the plating operation using this plating solution is based on a batch process, which is not suitable for a continuous plating operation, but this does not allow efficient plating.
一方、 .上記無電解白金めつき液よりも安定性が良好なものとして、 特開平 5 - 2 2 2 5 4 3号公報に記載の無電解白金めつきがある。 こ のめつき液は、 一般式 〔P t ( N H 3 ) 6 X〕 で表される 4価の白金ァ ンミン塩を主成分とするものであり、 安定化剤がなくとも連続的なめ つき処理に際して安定的に白金めつきを行なうことが可能であること が開示されている。 そして、 このめつき液によれば、 高品質の白金薄 膜を製造することができ、 またその光沢も良好であることから装飾品 のめつきにも適用可能であることが述べられている。 しかしながら、 特開平 5 - 2 2 2 5 4 3号公報に記載の無電解白金 めっき液もその安定性は必ずしも十分ではなく、 本発明者が予備的に 試験を行なったところ、 この従来のめっき液では分解を完全に抑制す ることができず、 めっき槽壁面へ白金が析出し膜厚制御が困難となる ことを確認している。 従って、 この無電解白金めつき液は、 厳密な厚 さの制御が必要な白金薄膜の製造には不向きであると考えられる。 近年、 白金のような貴金属の用途は拡大しており、 これまでの装飾 品、 触媒、 耐熱材料といった用途から、 半導体デバイスのキャパシ夕 一電極といった先端分野への利用が期待されている。 そして、 このよ うな分野で使用される白金薄膜を無電解めつきにて製造するためには、 従来の無電解めつき液はそのまま適用することができず、 より安定性 の優れた無電解白金めつき液の開発が望まれている。 本発明は以上のような背景の下になされたものであり、 安定性が極 めて高く連続的なめっき操業を可能とすると共に、 高品質の薄膜を製 造可能な無電解白金めつき液を提供することを目的とする。 そして、 このめつき液を用いためっき方法を提供することを目的とする。 発明の開示 On the other hand, one having better stability than the above electroless platinum plating liquid is electroless platinum plating described in JP-A-5-222543. This The plating solution is mainly composed of a tetravalent platinum amine salt represented by the general formula [Pt (NH 3 ) 6 X], and is used for continuous plating without a stabilizer. It is disclosed that platinum plating can be performed stably. According to this plating liquid, it is possible to produce a high-quality platinum thin film, and it is also applicable to the plating of decorative articles because of its good gloss. However, the stability of the electroless platinum plating solution described in Japanese Patent Application Laid-Open No. 5-222543 is not always sufficient, and the present inventor conducted preliminary tests. It was confirmed that decomposition could not be completely suppressed and that deposition of platinum on the plating tank wall surface made it difficult to control the film thickness. Therefore, this electroless platinum plating solution is considered to be unsuitable for the production of a platinum thin film requiring strict thickness control. In recent years, applications of precious metals such as platinum have been expanding, and they are expected to be used in advanced fields such as capacities of semiconductor devices, instead of decorative articles, catalysts, and heat-resistant materials. In order to produce a platinum thin film used in such fields by electroless plating, a conventional electroless plating solution cannot be applied as it is, and the more stable electroless platinum is used. The development of plating liquid is desired. The present invention has been made in view of the above background, and has extremely high stability, enables continuous plating operation, and has an electroless platinum plating solution capable of producing a high-quality thin film. The purpose is to provide. And it aims at providing the plating method using this plating solution. Disclosure of the invention
本発明者は、 上記したへキサァミノ白金錯体 (〔P t ( N H 3 ) 6 X〕) を主成分とする無電解白金めつき液の安定性を評価しつつ、 更にその 安定性を向上させるベく詳細な検討を行なつたところ、 このめつき液 は 4価のへキサアミノ白金錯体を主成分としているものの、 下記のよ うな不純物を含有していることを見出した。 式 1 The present inventor evaluated the stability of the electroless platinum plating solution containing the above hexaminoplatinum complex ([Pt (NH 3 ) 6 X]) as a main component, After a detailed study to improve the stability, it was found that this plating solution contained the following impurities, although it contained a tetravalent hexaaminoplatinum complex as a main component. Equation 1
[ P t C I ( a ) 53 3 + [P t CI (a) 5 3 3 +
[ P t C ( a ) J [P t C (a) J
[ P t C ( a ) 3 ] + [P t C (a) 3 ] +
[ P t ( a ) 4 ] 2 + [P t (a) 4 ] 2 +
このような、 不純物は原料となるへキサアミノ白金錯体塩の製造ェ 程、 めっき液の調製過程において生じるものであると考えられるが、 主成分であるへキサァミノ白金錯体に比して安定性に乏しく液中で分 解して、 めっき槽壁面や被めつき物に付着し易い白金微粒子を生じさ せる。 そして、 この白金微粒子の触媒作用によりめつき槽壁面や被め つき物のめっき部分以外の箇所で白金の析出が促進されるのである。 そこで、本発明者は、このめつき液の安定性を向上させるためには、 上記した不純物を排除することが必要であるとし、 そのためには、 め つき液の製造工程において、 へキサァミノ白金錯体を予め精製するの が適当であるとした。 そして、 その具体的手法として、 原料となるへ キサァミノ白金錯体塩を水溶液とし、 これに炭酸ガスを吹き込み、 一 旦、 精製目的となるへキサァミノ白金錯体の炭酸塩を製造し、 これか らへキサァミノ白金錯体を抽出する手法を見出した。 ここで、 このよ うに一度炭酸ガスと反応させることとしたのは、 炭酸イオンは精製目 的である 4価のへキサアミノ白金錯体に対する反応性及び選択性に優 れ、 これによりへキサアミノ白金錯体を高純度で抽出できるとの考え に基づくものである。 即ち、 本願発明は、 下記一般式で示されるへキサァミノ白金錯体の 塩を原料として、 前記へキサァミノ白金錯体を含む無電解白金めつき 液を製造する方法において、 以下の工程で示されるへキサァミノ白金 錯体の精製工程を含むことを特徴とする無電解白金めつき液の製造方 法である。 式 2 Such impurities are considered to be generated in the process of preparing the plating solution during the production of the hexaminoaminoplatinum complex salt used as the raw material, but are less stable than the hexaminoplatinum complex as the main component. It decomposes in the solution to produce platinum fine particles that easily adhere to the plating tank wall and the adherend. Then, the catalytic action of the platinum fine particles promotes the deposition of platinum on portions other than the plating tank wall surface and the plated portion of the adherend. Therefore, the present inventor has determined that in order to improve the stability of the plating solution, it is necessary to eliminate the above-mentioned impurities, and for that purpose, in the production process of the plating solution, a hexaminoplatinum complex was used. It was considered appropriate to purify in advance. As a specific method, a hexaneaminoplatinum complex salt as a raw material is made into an aqueous solution, and carbon dioxide gas is blown into the aqueous solution. A technique for extracting platinum complexes was found. Here, the reason for once reacting with the carbon dioxide gas is that the carbonate ions have excellent reactivity and selectivity with respect to the tetravalent hexaminoaminoplatinum complex to be purified. This is based on the idea that the hexaminoaminoplatinum complex can be extracted with high purity. That is, the present invention provides a method for producing an electroless platinum plating solution containing a hexaminoplatinum complex using a salt of the hexaminoplatinum complex represented by the following general formula as a raw material, A method for producing an electroless platinum plating solution, which comprises a step of purifying a complex. Equation 2
[P t (a) J 4 + [P t (a) J 4 +
(式中、 aは、 CnH2 n + 1NH2 (nは 0〜1 0の整数) で示される アミノ基を示す。) (Wherein, a is, C n H 2 n + 1 NH 2 (n is an amino group represented by 0 to 1 0 integer).)
(a) 原料となるへキサァミノ白金錯体塩を水溶液とし、 前記水溶液 に炭酸ガスを通過させ、 へキサァミノ白金錯体炭酸塩を製造する工程(a) a step of producing a hexaminoplatinum complex carbonate by converting a hexaminoplatinum complex salt as a raw material into an aqueous solution, and passing carbon dioxide gas through the aqueous solution;
(b) 前記へキサァミノ白金錯体炭酸塩を酸で溶解する工程 以下、 本発明の特徴となる精製工程について説明する。 本発明における精製工程では、 まず、 へキサァミノ白金錯体塩を水 溶液とする。 ここで、 へキサァミノ白金錯体塩としては、 水酸化物を 用いるのが好ましい。 これは、 その後の炭酸ガスと反応させて炭酸塩 とする工程において不純物の共沈が最も少ないからである。 一方、 こ の水溶液とする際のへキサアミノ白金錯体塩の溶解量としては、 白金 換算で 1 g/L〜20 gZLとするのが好ましい。 1 gZL未満では 十分な量の炭酸塩が精製せず、 また、 効率が悪いからである。 また、 20 gZLを超えると塩が溶解しないからである。 そして、 この水溶液に炭酸ガスを吹き込み、 炭酸塩を沈降させる。 ここで、 炭酸ガスの通過量については、 水溶液中のへキサァミノ白金 錯体塩溶液の濃度により異なるが、 その目安としては溶液が中性とな るまで炭酸ガスを吹き込むのが良い。 (b) Step of Dissolving the Hexamino Platinum Complex Carbonate with Acid Hereinafter, the purification step which is a feature of the present invention will be described. In the purification step of the present invention, first, a hexaminoplatinum complex salt is converted into an aqueous solution. Here, it is preferable to use a hydroxide as the hexamino platinum complex salt. This is because coprecipitation of impurities is the least in the subsequent step of reacting with carbon dioxide to form carbonate. On the other hand, the amount of the hexaaminoplatinum complex salt dissolved in the aqueous solution is preferably 1 g / L to 20 gZL in terms of platinum. If the amount is less than 1 gZL, a sufficient amount of carbonate cannot be purified, and the efficiency is low. Also, if it exceeds 20 gZL, the salt will not be dissolved. Then, carbon dioxide gas is blown into the aqueous solution to precipitate carbonates. The amount of carbon dioxide gas passing here depends on the concentration of the hexaminoplatinum complex salt solution in the aqueous solution. As a guide, it is better to blow carbon dioxide gas until the solution becomes neutral.
以上の操作により、 水溶液中のへキサアミノ白金錯体は炭酸塩とし て沈殿する。 この炭酸塩は上記した不純物を含まない高純度のへキサ アミノ白金錯体炭酸塩である。  By the above operation, the hexaminoaminoplatinum complex in the aqueous solution precipitates as a carbonate. This carbonate is a high purity hexaaminoplatinum complex carbonate that does not contain the above-mentioned impurities.
次にこの炭酸塩から白金めつきのためのへキサァミノ白金錯体ィォ ンを抽出すべく、 炭酸塩を酸で溶解する。 ここで、 炭酸塩を溶解させ る酸としては、 塩酸等のハロゲン酸類も炭酸塩を溶解することができ るが、 これらの酸を用いた場合、 溶解液中にハロゲンが残留し、 これ がめつき薄膜に吸着して析出速度を低下させると共に薄膜の外観を黒 くすることとなる。 また、 同様に、 硫酸は硫酸塩を生成することとな り、 硝酸は薄膜の外観を悪化させるという問題がある。  Next, the carbonate is dissolved with an acid in order to extract the hexaminoplatinum complex for platinum plating from the carbonate. Here, as an acid for dissolving the carbonate, a halogen acid such as hydrochloric acid can also dissolve the carbonate. However, when these acids are used, the halogen remains in the dissolution solution, and this is fixed. The thin film is adsorbed on the thin film, thereby decreasing the deposition rate and darkening the appearance of the thin film. Similarly, sulfuric acid generates sulfate, and nitric acid has a problem that the appearance of the thin film is deteriorated.
そこで、 本発明において適用する酸としては、 メタンスルホン酸、 エタンスルホン酸等の有機スルホン酸又は酢酸、 プロピオン酸等の低 分子量の有機カルボン酸を適用するのが好ましい。 尚、 これらの酸は 水溶液の状態で添加するものとする。 また、 この酸添加後の溶液中に は炭酸イオンが残留していることから、 めっき液の製造の際には、 炭 酸イオンを除去しておくことが望ましい。 この炭酸除去の方法として は、 炭酸塩を上記した有機スルホン酸又は有機カルボン酸等の酸に溶 解させる際に c o 2が発泡するので、 溶解時に溶液を減圧雰囲気にす ることにより容易に炭酸イオンは除去される。 Thus, as the acid used in the present invention, it is preferable to use an organic sulfonic acid such as methanesulfonic acid or ethanesulfonic acid, or a low molecular weight organic carboxylic acid such as acetic acid or propionic acid. These acids are added in the form of an aqueous solution. In addition, since carbonate ions remain in the solution after the addition of the acid, it is desirable to remove the carbonate ions when producing the plating solution. The method of this carbonate removal, since co 2 a carbonate in which dissolve in an acid such as an organic sulfonic acid or organic carboxylic acids described above can be foamed easily carbonate by to Rukoto reduced pressure atmosphere solution upon dissolution The ions are removed.
これらの精製工程後の水溶液は高純度のへキサアミノ白金錯体溶液 である。 そして、 このへキサァミノ白金錯体溶液はそのまま無電解白 金めつき液として利用もできるが、 白金錯体の濃度を所定の濃度とす るために適宜希釈して良く、 これにより本発明に係る無電解白金めつ き液とすることができる。  The aqueous solution after these purification steps is a high-purity hexaaminoplatinum complex solution. The hexaminoplatinum complex solution can be used as it is as an electroless platinum plating solution, but it may be appropriately diluted to bring the concentration of the platinum complex to a predetermined concentration. It can be a platinum plating liquid.
ここで、 この本発明に係る無電解白金めつき液については、 適宜に 還元剤を添加するのが好ましい。この還元剤としては、ホスフィン酸、 ホスホン酸、 ヒドラジン、 ボロンハイ ドライ ド、 ホルマリン、 L—ァ スコルビン酸、 ギ酸等が適用可能である。 これらの還元剤濃度として はめつき液中の白金イオン濃度 (モル濃度) の 1〜 1 0倍とするのが 好ましい。 Here, regarding the electroless platinum plating liquid according to the present invention, It is preferred to add a reducing agent. As this reducing agent, phosphinic acid, phosphonic acid, hydrazine, boron hydride, formalin, L-ascorbic acid, formic acid and the like are applicable. The concentration of these reducing agents is preferably 1 to 10 times the platinum ion concentration (molar concentration) in the plating solution.
また、 本発明に係るめっき液は高精度の薄膜を製造可能とするもの であるが、 モホロジ—に優れピットのない白金薄膜を製造するために は、 更に、 レべリング剤を添加するのが好ましい。 ここで、 レベリン グ剤は一般的な白金以外の無電解めつき液にも適用されることがあり、 この場合は陽イオン系の界面活性剤が適用されている。 しかし、 本発 明が製造目的とする白金薄膜はこれら界面活性剤中の有機物を吸着し 易く、 析出速度の低下や、 場合によっては析出反応の中断が生じる。 また、 これら界面活性剤を添加した際に不溶性の沈殿物が生じること がある。 そこで、 本発明の無電解めつき液のレべリング剤としては、 ポリオキシエチレンアルキルエーテル、 ポリアルキルフエニルエーテ ル、 ポリオキシエチレンポリオキシプロピルアルキルエーテル、 ダリ セリンエステル、 ポリグリセリンエステル、 ソルピ夕ンエステル等の 非イオン系界面活性剤を適用するのが好ましい。 そして、 これらのレ ベリング剤濃度としては 0 . 1〜 1 0 0 p p mとするのが好ましい。 本発明に係る無電解白金めつき液によれば、 めっき液の分解が生じ させることなく安定的な白金めつき処理が可能であり、 ステツプカバ レツジに優れると共に高精度の白金薄膜が製造可能である。 そして、 本発明に係る無電解白金めつき液を用いて白金めつきを行なう際の条 件としては、 p Hを 8〜 1 2とし、 液温を 4 0〜 8 0 °Cとするのが好 ましい。 p Hについては、 p H 8未満では白金の析出が生じないから であり、 p H 1 2を超えると作業環境が悪化するからである。 また、 液温については、 4 0 °C未満では白金が析出しないからであり、 8 0 °C を超えるとめつき液中のァミンの蒸発が著しくなるからである。 尚、 このめつき液の p Hを調整する際には、 めっき液に酸又はアル力リを 添加することとなるが、 アルカリを添加する際には、 へキサァミノ白 金錯体において白金に配位しているアミノ基 (化 3の a) と同じアミ ノ基を有するアル力リを適用するのが好ましい。 Further, the plating solution according to the present invention enables the production of a high-precision thin film. However, in order to produce a platinum thin film having excellent morphology and no pits, it is necessary to further add a leveling agent. preferable. Here, the leveling agent may be applied to a general electroless plating solution other than platinum. In this case, a cationic surfactant is applied. However, the platinum thin film intended for the production of the present invention tends to adsorb the organic substances in these surfactants, so that the deposition rate is reduced and, in some cases, the deposition reaction is interrupted. When these surfactants are added, insoluble precipitates may be formed. Therefore, as the leveling agent for the electroless plating solution of the present invention, polyoxyethylene alkyl ether, polyalkylphenyl ether, polyoxyethylene polyoxypropyl alkyl ether, dalyserine ester, polyglycerin ester, sorbitan ester It is preferable to use a nonionic surfactant such as ester. The concentration of these leveling agents is preferably 0.1 to 100 ppm. ADVANTAGE OF THE INVENTION According to the electroless platinum plating solution which concerns on this invention, a stable platinum plating process is possible without decomposing | disassembling a plating solution, and it is excellent in step coverage and can manufacture a highly precise platinum thin film. . The conditions for performing platinum plating using the electroless platinum plating solution according to the present invention are as follows: pH is set to 8 to 12, and the liquid temperature is set to 40 to 80 ° C. It is good. This is because, when the pH is less than pH 8, precipitation of platinum does not occur, and when the pH exceeds pH 12, the working environment deteriorates. In addition, when the liquid temperature is lower than 40 ° C, platinum does not precipitate, and when the liquid temperature is higher than 80 ° C, evaporation of amine in the plating liquid becomes remarkable. When adjusting the pH of this plating solution, add acid or aluminum to the plating solution. When adding the alkali, it is necessary to apply an alkali having the same amino group as the amino group (a in Chemical formula 3) coordinated to platinum in the hexamino platinum complex. Is preferred.
また、 このめつき処理においては、 薄膜形成を行ないたい箇所に対 して成長源として白金を蒸着する触媒付与処理を行なうことが好まし い。 この際の触媒付与処理で蒸着する白金は極めて薄いもので良い。 発明を実施するための最良の形態  In addition, in this plating process, it is preferable to perform a catalyst application process of depositing platinum as a growth source on a portion where a thin film is to be formed. At this time, the platinum deposited by the catalyst application treatment may be extremely thin. BEST MODE FOR CARRYING OUT THE INVENTION
以下、 本発明の好適な実施形態を比較例と共に説明する。 第 1実施形態 : 白金濃度で 1 0 gZLの「P t (NH3) 6] (OH) 4 溶液を 5 L用意し、この溶液に炭酸ガスを 3時間吹き込んだ。そして、 沈殿した炭酸塩をろ過採取しこれを洗浄、 乾燥した。 次に、 含有白金 量が 3 0 gとなるようにこの炭酸塩を秤量し、 これに酢酸 4 5 mLを 添加して炭酸塩を溶解し更に水を加えて液量を 1 Lとした後、 溶解後 の溶液を減圧して炭酸を除去した。 Hereinafter, preferred embodiments of the present invention will be described together with comparative examples. First Embodiment: 5 L of a “Pt (NH 3 ) 6 ] (OH) 4 solution having a platinum concentration of 10 gZL was prepared, and carbon dioxide gas was blown into the solution for 3 hours. The carbonate was weighed so that the amount of platinum contained was 30 g, and 45 mL of acetic acid was added thereto to dissolve the carbonate, and further water was added. Then, the solution after dissolution was reduced in pressure to remove carbonic acid.
このようにして精製したへキサァミノ白金錯体溶液( [P t (NH3) 6] (C H3 C O O) 4溶液) から、 白金量 3 g分の溶液 ( 1 0 OmL) を採取し、 これに還元剤としてヒドラジン一水和物 3 mLを加え、 溶 液の p Hが p H 1 1となるように 2 8 %アンモニア水を 7 O mL添加 した後、 液量 1 Lとなるように脱イオン水を添加し、 更に、 レベリン グ剤としてグリセリンエステル 2 0 p pmを添加した。 This way Kisaamino platinum complex solution to the purified ([P t (NH 3) 6] (CH 3 COO) 4 solution) was taken platinum amount 3 g portion of the solution (1 0 OML), reduced to this Add 3 mL of hydrazine monohydrate as an agent, add 7 O mL of 28% aqueous ammonia so that the pH of the solution becomes pH 11, and then add deionized water so that the volume becomes 1 L. Was added, and glycerin ester (20 ppm) was further added as a leveling agent.
以上のようにして製造した無電解白金めつき液を液温 6 0 °Cとして 'これに触媒付与処理を施したアルミナ板を浸漬して白金めつき処理を 行なった。 この結果、 析出速度 1 : 8 mZhで光沢の良好な白金が 析出した。 また、 このめつき処理後のめっき液を 1週間放置したが、 めっき液の分解は生じないことが確認された。 第 2実施形態 : 白金濃度で 1 0 gZLの [P t (NH3) 6] (OH) 4 を 5 L用意し、 この溶液に炭酸ガスを 3時間吹き込んだ。 そして、 沈 殿した炭酸塩をろ過採取しこれを洗浄、 乾燥した。 次に、 炭酸塩にメ 夕ンスルホン酸 5 0 mLを添加して炭酸塩を溶解し更に水を加えて液 量を 1 Lとした後、 溶液から炭酸を除去した。 The electroless platinum plating solution produced as described above was heated to a temperature of 60 ° C., and an alumina plate treated with a catalyst was immersed in the solution to perform platinum plating. As a result, platinum with good gloss was deposited at a deposition rate of 1: 8 mZh. The plating solution after the plating treatment was left for one week, but it was confirmed that the plating solution did not decompose. Second Embodiment: [P t (NH 3) 6] in 1 0 GZL platinum concentration (OH) 4 Was prepared, and carbon dioxide gas was blown into the solution for 3 hours. The precipitated carbonate was collected by filtration, washed, and dried. Next, 50 mL of maleic sulfonic acid was added to the carbonate to dissolve the carbonate, and water was further added to make the volume 1 L, and then the carbonic acid was removed from the solution.
そして、 この白金錯体溶液から、 白金量 3 g分の溶液 ( 1 0 0 mL) を採取し、 還元剤としてヒドラジン一水和物 3mLを加え、 溶液 pH が p H 1 0. 5となるように 2 8 %アンモニア水を 7 0 mL添加した 後、 液量 1 Lとなるように脱イオン水を添加し、 更に、 レべリング剤 としてポリォキシエチレンドデシルエーテル 2 0 p pmを添加した。 第 1実施形態と同様、 液温 6 0°Cとしてアルミナ板に白金めつき処 理を行なった。 この結果、 析出速度 1. 3 zm/hで光沢の良好な白 金が析出した。 また、 このめつき処理後のめっき液も 1週間放置後の めっき液の分解は生じないことが確認された。 第 3実施形態:本実施形態では、 第 2実施形態と同様、 [P t (NH3) 6] (OH) 4水溶液を原料として炭酸塩を製造し、 これに第 2実施形 態のメタンスルホン酸に替えて、 エタンスルホン酸を 6 OmL添加し て炭酸塩を溶解し、 還元剤、 を添加し、 pH調整、 液量調整を行ない めっき液を製造した。 ここでの、 [P t (NH3) 6] (OH) 4の濃度 等のその他の条件は第 2実施形態と同様である。 Then, a solution (100 mL) of 3 g of platinum was collected from the platinum complex solution, and 3 mL of hydrazine monohydrate was added as a reducing agent to adjust the solution pH to pH 10.5. After 70 mL of 28% aqueous ammonia was added, deionized water was added so as to have a liquid volume of 1 L, and polyoxyethylene dodecyl ether 20 ppm as a leveling agent was further added. As in the case of the first embodiment, a platinum plating treatment was performed on an alumina plate at a liquid temperature of 60 ° C. As a result, platinum with good gloss was deposited at a deposition rate of 1.3 zm / h. It was also confirmed that the plating solution after the plating treatment did not decompose after leaving it for one week. Third Embodiment: In this embodiment, as in the second embodiment, a carbonate is produced using an aqueous solution of [Pt (NH 3 ) 6 ] (OH) 4 as a raw material. In place of the acid, 6 OmL of ethanesulfonic acid was added to dissolve the carbonate, and a reducing agent was added to adjust the pH and the volume of the solution to produce a plating solution. Here, other conditions such as the concentration of [Pt (NH 3 ) 6 ] (OH) 4 are the same as in the second embodiment.
そして、 ここでも液温 6 0 °Cとして、 アルミナ板に白金めつき処理 を行なった結果、 析出速度 1. 1 mZhで光沢の良好な白金が析出 した。 また、 このめつき処理後のめっき液も 1週間放置後のめっき液 の分解は生じないことが確認された。 第 4実施形態:本実施形態では、 第 2実施形態の [P t (NH3) 6] (O H) 4に替えてへキサァミノ白金錯体塩として、 白金濃度 l O gZL の [P t (CH3NH2) 6] (OH) 45 Lを用いた。 そして、 第 2実施 形態と同様の条件で炭酸ガスを吹き込み、 採取した炭酸塩にエタンス ルホン酸を添加して炭酸塩を溶解し、 この溶液を 1 0 0 mL採取して 還元剤を添加し、 p H調整、 液量調整を行ないめつき液を製造した。 尚、 還元剤の量等の条件は第 2実施形態と同様である。 Again, at a liquid temperature of 60 ° C., platinum plating was performed on the alumina plate, and as a result, platinum with a good gloss was deposited at a deposition rate of 1.1 mZh. It was also confirmed that the plating solution after the plating treatment did not decompose after leaving it for one week. Fourth Embodiment: In this embodiment, instead of [Pt (NH 3 ) 6 ] (OH) 4 in the second embodiment, as a hexaminoplatinum complex salt, a platinum concentration l O gZL of [P t (CH 3 NH 2) 6] (OH) was used 4 5 L. Then, carbon dioxide gas is blown under the same conditions as in the second embodiment, and ethane ethane is added to the collected carbonate. Rubonic acid was added to dissolve the carbonate, 100 mL of this solution was sampled, and a reducing agent was added to adjust the pH and the volume of the solution to produce a plating solution. The conditions such as the amount of the reducing agent are the same as in the second embodiment.
そして、 液温 6 0°Cとして、 アルミナ板に白金めつき処理を行なつ た結果、 析出速度 1. 0 mZhで光沢の良好な白金が析出した。 ま た、 このめつき処理後のめっき液も 1週間放置後のめっき液の分解は 生じないことが確認された。 第 5実施形態 :本実施形態では、 第 4実施形態で精製した  Then, at a liquid temperature of 60 ° C., platinum plating was performed on the alumina plate, and as a result, platinum with a good gloss was deposited at a deposition rate of 1.0 mZh. It was also confirmed that the plating solution after the plating treatment did not undergo decomposition of the plating solution after standing for one week. Fifth Embodiment: In the present embodiment, the purification is performed in the fourth embodiment.
ノ白金錯体溶液 1 0 OmLに還元剤としてホスフィン酸 2 0 gを加え た後、 溶液 pHが pH 8. 0となるように調製して液量 1 Lとなるよ うに脱イオン水を添加し、 更に、 レべリング剤としてポリオキシェチ レンドデシルエーテル 2 0 p pmを添加した。 After adding 20 g of phosphinic acid as a reducing agent to 10 OmL of the noplatinum complex solution, adjust the solution pH to pH 8.0, and add deionized water so that the solution volume becomes 1 L. Furthermore, 20 ppm of polyoxyethylene blended ether was added as a leveling agent.
そして、 このめつき液を用いて液温 8 0°Cとして、 アルミナ板に白 金めつき処理を行なった結果、 析出速度 0. 9 5 zmZhで光沢の良 好な白金が析出した。 また、 このめつき処理後のめっき液も 1週間放 置後のめつき液の分解は生じないことが確認された。 比較例:上記した実施形態に対する比較例として、 原料として第 1実 施形態と同様の [P t (NH3) 6] (OH) 4を用い、 精製工程を経る ことなくこれから直接めつき液を製造し、 その安定性を検討した。 こ の比較例では、 白金濃度 1 0 gZLの [P t (NH3) 6 ] (OH) 4溶 液 1 Lに、 還元剤としてヒドラジン一水和物 3 m Lとグリシン 0. 2 gとを加え、 安定化剤として一酸化鉛 0. 2mgを加えた。 そして、 液量を調整し、 p Hを p H 1 2に調製してめっき液とした。 Then, the alumina plate was subjected to a platinum plating treatment at a liquid temperature of 80 ° C. using this plating solution. As a result, platinum having a good gloss was deposited at a deposition rate of 0.95 zmZh. It was also confirmed that the plating solution after the plating treatment did not decompose after leaving for one week. Comparative Example: As a comparative example with respect to the above-described embodiment, the same [Pt (NH 3 ) 6 ] (OH) 4 as in the first embodiment was used as a raw material, and the plating solution was directly used without going through a purification step. It was manufactured and its stability was studied. In this comparative example, 3 mL of hydrazine monohydrate and 0.2 g of glycine were used as reducing agents in 1 L of a [Pt (NH 3 ) 6] (OH) 4 solution having a platinum concentration of 10 g ZL. In addition, 0.2 mg of lead monoxide was added as a stabilizer. Then, the solution volume was adjusted, and the pH was adjusted to pH 12 to obtain a plating solution.
そして、 このめつき液を液温 6 0 °Cとして、 アルミナ板に白金めつ き処理を行なった結果、 析出速度は 2. 0 m_/hと第 1〜第 5実施 形態と比べて劣らない析出速度がえられたが、 めっき処理後のめっき 液を放置したところ、 1 日後にはめつき槽の底及び壁面に白金が析出 しているのが確認された。 これは、 比較例では安定剤を添加している にもかかわらず、 原料である [P t (NH3) 6] (OH) 4の精製を行 なわなかったため、 これに含まれていた不純物によりめつき液が分解 したためと考えられる。 産業上の利用可能性 The plating rate was 2.0 m_ / h, which was not inferior to those of the first to fifth embodiments. Deposition speed was obtained, but when the plating solution after the plating treatment was allowed to stand, platinum was deposited on the bottom and wall of the plating tank one day later. Was confirmed. This is because, although the stabilizer was added in the comparative example, the raw material [Pt (NH 3 ) 6 ] (OH) 4 was not purified, and the impurities contained therein caused the purification. It is considered that the plating liquid was decomposed. Industrial applicability
以上説明したように、 本発明は従来のへキサアミノ白金錯体を主成 分とする無電解白金めつき液の安定性を更に向上させるベく、 へキサ ァミノ白金錯体の精製を行なう無電解白金めつき液の製造方法であり、 これにより不純物を含まず、 めっき操業中の液組成の分解のない極め て安定な無電解白金めつき液が得られる。 そして、 本発明に係る無電 解白金めつき液によれば、 その安定性から高品質の白金薄膜を製造す ることができる。  As described above, the present invention aims to further improve the stability of a conventional electroless platinum plating solution containing a hexaminoaminoplatinum complex as a main component, and to improve the stability of an electroless platinum plating solution for purifying a hexaminoplatinum complex. This is a method of producing an electroless platinum plating solution, which does not contain impurities and does not decompose the composition of the solution during the plating operation. According to the electroless platinum plating solution of the present invention, a high-quality platinum thin film can be produced from its stability.

Claims

請求の範囲 The scope of the claims
1. 下記一般式で示されるへキサァミノ白金錯体の塩を原料として、 前記へキサァミノ白金錯体を含む無電解白金めつき液を製造する方法 において、 1. A method for producing an electroless platinum plating solution containing a hexaminoplatinum complex, using a salt of a hexaminoplatinum complex represented by the following general formula as a raw material,
式 1 Equation 1
[P t (a) 6] 4 + [P t (a) 6 ] 4 +
(式中、 aは、 CnH2 n + 1NH2 (nは 0〜 1 0の整数) で示される アミノ基を示す。) (Wherein, a is, C n H 2 n + 1 NH 2 (n is an amino group represented by 0-1 0 integer).)
下記工程で示されるへキサアミノ白金錯体の精製工程を含むことを 特徴とする無電解白金めつき液の製造方法。  A method for producing an electroless platinum plating solution, comprising a step of purifying a hexaaminoplatinum complex shown in the following step.
( a) 原料となるへキサァミノ白金錯体塩を水溶液とし、 前記水溶液 に炭酸ガスを通過させ、 へキサァミノ白金錯体炭酸塩を製造する工程 (a) a step of producing a hexaminoplatinum complex carbonate by converting a hexaminoplatinum complex salt as a raw material into an aqueous solution and passing carbon dioxide gas through the aqueous solution;
(b) 前記へキサァミノ白金錯体炭酸塩を酸で溶解する工程 (b) dissolving the hexaminoplatinum complex carbonate with an acid
2. ( a) 工程のへキサアミノ白金錯体塩として、 水酸化物を用いる請 求項 1記載の無電解白金めつき液の製造方法。 2. The method for producing an electroless platinum plating liquid according to claim 1, wherein a hydroxide is used as the hexaminoaminoplatinum complex salt in the step (a).
3. (b) 工程の酸として、 有機スルホン酸又は分子量 3 0 0以下の有 機カルボン酸を用いる請求項 1又は請求項 2記載の無電解白金めつき 液の製造方法。 3. The method for producing an electroless platinum plating liquid according to claim 1, wherein an organic sulfonic acid or an organic carboxylic acid having a molecular weight of 300 or less is used as the acid in the step (b).
4. 請求項 1〜請求項 3記載の方法により製造される無電解白金めつ さ液。 4. An electroless platinum plating liquid produced by the method according to claim 1.
5. 還元剤として、 ホスフィン酸、 ホスホン酸、 ヒドラジン、 ボロン ハイ ドライ ド、 ホルマリン、 Lーァスコルビン酸、 ギ酸の少なくとも いずれかを含む請求項 4記載の無電解白金めつき液。 5. The electroless platinum plating solution according to claim 4, wherein the reducing agent contains at least one of phosphinic acid, phosphonic acid, hydrazine, boron hydride, formalin, L-ascorbic acid, and formic acid.
6. レべリング剤として、 非イオン系界面活性剤を含む請求項 4又は 請求項 5記載の無電解白金めつき液。 6. The electroless platinum plating liquid according to claim 4, which contains a nonionic surfactant as a leveling agent.
7. 請求項 4〜請求項 6記載の無電解白金めつき液と被めつき物とを 接触させる無電解白金めつき方法であって、 7. A method for plating electroless platinum, which comprises bringing the electroless platinum plating liquid according to claim 4 into contact with an object to be plated,
前記無電解白金めつき液の p Hを p H 8〜 l 2、 液温を 4 0〜 8 0 °Cとして被めつき物とを接触させる無電解白金めつき方法。  An electroless platinum plating method in which the pH of the electroless platinum plating liquid is set at pH 8 to l2 and the temperature of the liquid is 40 to 80 ° C, and the substance is brought into contact with the object to be plated.
PCT/JP2001/010608 2000-12-05 2001-12-05 Process for producing plating solution for electroless platinum plating, plating solution for electroless platinum plating, and method of electroless platinum plating WO2002046492A1 (en)

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JPH05222543A (en) * 1992-02-14 1993-08-31 Electroplating Eng Of Japan Co Electroless platinum plating bath and production of platinum plated product using the same
EP1024211A2 (en) * 1999-01-19 2000-08-02 Shipley Company LLC Silver alloy plating bath and a method of forming a silver alloy film by means of the same

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05222543A (en) * 1992-02-14 1993-08-31 Electroplating Eng Of Japan Co Electroless platinum plating bath and production of platinum plated product using the same
EP1024211A2 (en) * 1999-01-19 2000-08-02 Shipley Company LLC Silver alloy plating bath and a method of forming a silver alloy film by means of the same

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