EP0423005A1 - Hydrazinbad zur stromlosen Plattierung mit Platin und/oder Palladium, sowie Verfahren zur Herstellung eines solchen Bades - Google Patents

Hydrazinbad zur stromlosen Plattierung mit Platin und/oder Palladium, sowie Verfahren zur Herstellung eines solchen Bades Download PDF

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Publication number
EP0423005A1
EP0423005A1 EP90402778A EP90402778A EP0423005A1 EP 0423005 A1 EP0423005 A1 EP 0423005A1 EP 90402778 A EP90402778 A EP 90402778A EP 90402778 A EP90402778 A EP 90402778A EP 0423005 A1 EP0423005 A1 EP 0423005A1
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EP
European Patent Office
Prior art keywords
bath
palladium
ethylenediamine
platinum
solution
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.)
Withdrawn
Application number
EP90402778A
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English (en)
French (fr)
Inventor
Pierre Josso
Serge Alperine
Pierre Steinmetz
Anne Costantini-Friant
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.)
Office National dEtudes et de Recherches Aerospatiales ONERA
Original Assignee
Office National dEtudes et de Recherches Aerospatiales ONERA
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Publication date
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Publication of EP0423005A1 publication Critical patent/EP0423005A1/de
Withdrawn legal-status Critical Current

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Classifications

    • 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 invention relates to the chemical deposition of platinum and / or palladium on a substrate, by autocatalytic reduction.
  • the industrial utility of a metal deposition bath depends to a large extent on the following three parameters: - absence of annoying impurities in the deposit; - Possibility of obtaining deposits with a thickness of several microns in a reasonable time, which implies both autocatalytic properties and a deposition rate of several microns per hour; - long bath life, preferably unlimited with periodic refills.
  • European Patent 0 227 518 in the name of the Applicant relating to a nickel and / or cobalt deposition bath, explains the advantage of choosing hydrazine as a reducing agent, which does not provide any impurity in the deposit.
  • This same patent also indicates that many anions, and in particular chloride, sulfate and nitrate anions, disturb the functioning of hydrazine baths.
  • US Patent No. 3,562,911 describes hydrazine baths for the chemical deposition of platinum, containing hexachloroplatinic acid and hydrochloric acid, and therefore chloride ions. These baths are not autocatalytic and operate until exhaustion without the reaction can be stopped. The platinum yield is at most 91%, that is to say that at least 9% of the platinum ions contained in the bath are lost.
  • the object of the invention is to provide a hydrazine autocatalytic bath, not containing chloride ions and which can be recharged to operate for long periods of time.
  • the subject of the invention is an aqueous bath for the chemical deposition of platinum and / or palladium, containing a compound of the metal or of each of the metals to be deposited and of hydrazine as reducing agent, characterized in that said compound is an oxalate and that the bath contains ethylenediamine as complexing agent and at least one stabilizer, this bath being strongly basic and having an autocatalytic action.
  • a bath according to the invention for the deposition of platinum advantageously contains platinum II at a concentration of between 0.05 and 0.15 g / l ion approximately, and a bath for the deposition of palladium, palladium at a concentration between 0.01 and 0.3 ion g / l approximately.
  • the invention also relates to a method for preparing a bath as defined above, in which a mother solution containing platinum II or palladium, ethylenediamine and oxalate anions is first prepared and therein then add the stabilizer (s) and hydrazine.
  • the platinum, ethylenediamine and oxalate concentrations and the pH of the stock solution are substantially the same as for the final bath.
  • the mother solution is concentrated, that is to say that the palladium ions, ethylenediamine and the oxalate anions are present there at higher concentrations than in the bath, and the stock solution is diluted and its pH possibly adjusted before introduction of the stabilizer and hydrazine.
  • a stock solution containing platinum, a stock solution containing palladium and dilution water are mixed in an amount suitable for obtaining the desired concentrations of platinum and palladium, and the stabilizer (s) and hydrazine are added.
  • Platinum II compounds and Platinum IV compounds are commercially available. The latter are much more stable and therefore easier to handle than the former. Their industrial use therefore leads to lower costs.
  • the most common platinum IV compounds are hexachloroplatinic acid H2PtCl6 and hexahydroxoplatinic acid H2Pt (OH) 6.
  • An intermediate complex is therefore formed with oxalate ions in an acid medium.
  • the acid medium suppresses the repulsive electrostatic effect with the amino ligand.
  • the platinum-ethylenediamine complex is obtained by neutralizing the acidic solution of platinum oxalate II by an excess of anhydrous ethylenediamine.
  • the pH can then be adjusted to a higher value by adding potassium hydroxide.
  • the manufacturing of the palladium stock solution uses palladium chloride PdCl2, which is the only compound practically available, as starting material.
  • This salt is soluble in an aqueous solution of hydrochloric acid.
  • a solution of potassium hydroxide in an amount sufficient to obtain a pH greater than 8 is added to the solution obtained, so as to precipitate the palladium in the form of hydroxide Pd (OH) 2, which is collected by filtration under vacuum.
  • This solution is neutralized by adding anhydrous ethylenediamine to a pH of about 10.
  • the mother solution is thus obtained in which the palladium is complexed with ethylenediamine.
  • This solution is concentrated and contains at least 0.1 gram ion of palladium, or at least 10 g / l of palladium metal.
  • the procedure for obtaining a palladium bath is as follows: - Diluted with deionized water, to the desired volume of bath, a volume of stock solution containing the desired amount of palladium ions. - We put in solution a primary stabilizer, for example arsenic pentoxide. - One or more secondary stabilizers chosen from imidazole, benzotriazole, copper sulphate, lead acetate, iodic acid and glycine are placed in solution. - The reducing agent (hydrated hydrazine) is added.
  • the mother solution obtained contains, for 1 liter, 0.1 gram ion of platinum, 1.2 mole of ethylenediamine and approximately 0.1 gram ion of oxalate.
  • a typical concentrated stock solution contains, for 1 liter, 0.1 to 0.2 gram ion of palladium and 0.1 to 0.19 gram ion of oxalate, its pH being between 9 and 12, depending on the quantities of reagent used and the final degree of concentration.
  • the ethylenediamine concentration is adjusted to 1M.
  • Example 1 To the stock solution of Example 1, the following constituents are added at the following concentrations: - primary stabilizer: arsenic pentoxide 6,5.10 ⁇ 4M - secondary stabilizer: imidazole 0.3M - reducing agent: hydrazine hydrate 1M
  • the pH of this bath is 13. It is used at 90 ° C. to coat an IN100 nickel-based alloy plate of dimensions approximate 10 mm x 13 mm x 2 mm. A constant deposition rate of 1 micron / hour is obtained for 2 hours, by recharging the bath periodically, after dosing, in a known manner. The deposit obtained is light gray and semi-gloss. Its surface appearance is dense and nodular, observations confirmed by metallographic examination on a polished section.
  • a bath is prepared having the following composition: Pt 0.1 ethylenediamine 3.1 oxaldate About 0.1 (remaining amount after precipitation) potassium hydroxide QSPP pH greater than 13 arsenic pentoxide 6.5 10 ⁇ 4 imidazole 0.5 hydrated hydrazine 4.1
  • the treated substrate is a Z10 NCD18-10 stainless steel plate previously nickel-plated and measuring approximately 20 mm x 20 mm x 2 mm. At a temperature of 82 ° C., a deposition rate of 1 micron / hour is obtained for 1 hour 40 minutes.
  • Example 2 From the stock solution of Example 2, a bath is prepared having the following composition in molarities: palladium 0.02 ethylenediamine 1.5 oxalate 0.19 arsenic pentoxide 10 ⁇ 3 imidazole 0.2 hydrazine 1 The pH of this bath is 10.5.
  • This bath is used to coat a nickel plate measuring approximately 10 mm x 10 mm x 2 mm at the temperature of 70 ° C. The speed obtained is 2 microns / hour for 1 hour.
  • the bath differs from the previous one in that the ethylenediamine concentration is 2M.
  • the concentration of ethylenediamine in the bath is brought to 3M, all other things being equal.
  • the deposition rate is 4 microns / hour for 1 hour.
  • the bath is similar to the previous ones, the ethylenediamine concentration being brought to 4M.
  • the deposition rate at 70 ° C goes to 5 microns / hour for 1 hour.
  • Example 5 A bath similar to that of Example 5 is prepared, except with regard to the imidazole concentration which is 0.3M.
  • the bath differs from those of Examples 1 and 9 by an imidazole concentration of 0.4M.
  • the concentration of imidazole in the bath is brought to 0.5M, without any other change.
  • the deposition rate increases to 4.5 microns / hour for 2 hours.
  • Example 2 From the stock solution of Example 2, a bath is prepared having the following composition, in molarities: palladium 0.1 ethylenediamine 3 oxalate 0.5 arsenic pentoxide 10 ⁇ 3 imidazole 0.4 hydrazine 1 Its pH is equal to 9.
  • the bath differs from that of Example 12 by replacing the arsenic pentoxide with copper sulphate at a concentration of 1.7.10 ⁇ 4M, the pH being equal to 9.5.
  • the bath differs from that of Example 12 by replacing the arsenic pentoxide with potassium iodate at the same concentration, the pH here again being equal to 9.5.
  • the bath differs from that of the previous example in that the potassium iodate concentration is reduced to 10 ⁇ 4M.
  • a deposition rate of 2.5 microns / hour for 10 hours is observed under the usual conditions of use.
  • the bath differs from those of the two previous examples in that the potassium iodate concentration is reduced to 10 ⁇ 5M.
  • the same bath at a temperature of 60 ° C provided a deposition rate of 1.5 microns / hour for 3 hours.
  • a bath is prepared having the following composition, in molarities: palladium 0.19 ethylenediamine 1 oxalate 0.19 arsenic pentoxide 6.5.10 ⁇ 4 imidazole 0.3 hydrazine 0.14 the pH being brought to a value greater than or equal to 13 by potassium hydroxide.
  • This bath can be used in a temperature range from 75 to 90 ° C, the deposition rate varying between 4 and 25 microns / hour.
  • the deposit obtained, whose growth is of the columnar type, has a very healthy surface appearance and slightly cracked in its external part (rapid growth deposit).
  • the bath of Example 16 is used to coat a plate te silicon carbide ceramic measuring approximately 10 mm x 8 mm x 3 mm having previously undergone an appropriate surface treatment.
  • this surface treatment comprises the following stages: a) chemical degreasing for 10 min in a solution having the following composition, at 90 ° C: sodium hydroxide 120 g / l trisodium phosphate 100 g / l sodium perborate NaBO2.H2O2.H2O 50 g / l wetting agent (Teepol type) 100 ml / l b) After careful rinsing with deionized water, immersion in a hydrochloric solution containing 5 g / l of palladium chloride, for 10 to 15 minutes. c) Rinsing again with deionized water then immersion in pure hydrated hydrazine for 3 to 5 minutes. d) Rinsing again with deionized water.
  • the wafer is then introduced into the bath according to the invention and the deposition reaction starts as soon as its surface temperature reaches that of the bath.
  • a deposition rate of 4.5 microns / hour is obtained for 2 hours.
  • the deposit is healthy and adherent.
  • a bath is prepared having the following composition, in molarities: palladium 0.03 platinum II 0.06 ethylenediamine 2.7 oxalate 0.2 arsenic pentoxide 10 ⁇ 3 imidazole 0.4 hydrazine 1
  • the pH of this bath is equal to 10.5. Under the conditions of use of Examples 5 to 15, a deposition rate of 3 microns / hour for 1 hour is obtained. Analysis of the deposit shows that it is an alloy composed of 80% palladium and 20% platinum by mass.
  • the baths according to the invention have a practically unlimited lifetime with periodic recharging.
  • Tables 1 and 2 indicate the ranges of compositions and conditions of use of the platinum and palladium baths respectively.
  • the load of the bath is the ratio between the surface to be coated and the volume of the bath.
  • the minimum and maximum columns indicate the limit values.
  • the "optimal" column indicates the preferred value or range of values for each parameter.
  • the stability of the baths according to the invention makes it possible to introduce therein particles to be included in the deposits, as described in the aforementioned Patent No. 2,590,595.
  • These particles (ceramic such as alumina or yttrine, metal or alloy) are obtained by grinding in the presence of the mother solution and a deflocculant.

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemically Coating (AREA)
EP90402778A 1989-10-11 1990-10-05 Hydrazinbad zur stromlosen Plattierung mit Platin und/oder Palladium, sowie Verfahren zur Herstellung eines solchen Bades Withdrawn EP0423005A1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8913294A FR2652822B1 (fr) 1989-10-11 1989-10-11 Bain a l'hydrazine pour le depot chimique de platine et/ou de palladium, et procede de fabrication d'un tel bain.
FR8913294 1989-10-11

Publications (1)

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EP0423005A1 true EP0423005A1 (de) 1991-04-17

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EP90402778A Withdrawn EP0423005A1 (de) 1989-10-11 1990-10-05 Hydrazinbad zur stromlosen Plattierung mit Platin und/oder Palladium, sowie Verfahren zur Herstellung eines solchen Bades

Country Status (4)

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US (1) US5085693A (de)
EP (1) EP0423005A1 (de)
JP (1) JPH03134178A (de)
FR (1) FR2652822B1 (de)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5882736A (en) * 1993-05-13 1999-03-16 Atotech Deutschland Gmbh palladium layers deposition process
DE102005046351A1 (de) * 2005-09-28 2007-04-05 Knorr-Bremse Systeme für Nutzfahrzeuge GmbH Bremsbelag, insbesondere für eine Scheibenbremse eines Nutzfahrzeugs
US9101915B2 (en) 2012-12-18 2015-08-11 Umicore Ag & Co. Kg Catalyst particles comprising a layered core-shell-shell structure and method of their manufacture
US9440224B2 (en) 2012-12-18 2016-09-13 Umicore Ag & Co. Kg Catalyst particles comprising hollow multilayered base metal-precious metal core/shell particles and method of their manufacture

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AUPN705195A0 (en) * 1995-12-08 1996-01-11 Cardiac Crc Nominees Pty Limited Electroless deposition of metallic coatings on non-conducting substrates
FR2787472B1 (fr) 1998-12-16 2001-03-09 Onera (Off Nat Aerospatiale) Procede pour produire une poudre d'alliage metallique de type mcraly et revetements obtenus avec cette poudre
KR20070118073A (ko) * 2005-01-12 2007-12-13 유미코아 갈바노테히닉 게엠베하 팔라듐층들을 증착하는 방법 및 이를 위한 팔라듐 배스
JP4662039B2 (ja) * 2005-07-08 2011-03-30 上村工業株式会社 ダイレクトプレーティング方法
JP5327494B2 (ja) * 2005-11-16 2013-10-30 日立化成株式会社 無電解めっき用触媒濃縮液の製造方法とそれを用いためっき触媒付与方法
DE102006029947B4 (de) * 2006-06-29 2013-01-17 Basf Se Verfahren zum Aufbringen einer metallischen Deckschicht auf einen Hochtemperatursupraleiter
EP2080822B1 (de) * 2006-11-06 2017-03-29 C. Uyemura & Co., Ltd. Verfahren zur direkten metallabscheidung und lösung zur bildung einer palladiumleiterschicht
JP2008184679A (ja) * 2007-01-31 2008-08-14 Okuno Chem Ind Co Ltd 無電解パラジウムめっき用活性化組成物
JP6012132B2 (ja) * 2011-12-20 2016-10-25 メタローテクノロジーズジャパン株式会社 無電解白金めっき液、その製造方法、及び白金皮膜の形成方法
DE102013207045A1 (de) * 2012-10-05 2014-06-12 Heraeus Precious Metals Gmbh & Co. Kg Verfahren zur Herstellung von Edelmetalloxalat-Komplexen
JP6352879B2 (ja) * 2015-10-15 2018-07-04 小島化学薬品株式会社 無電解白金めっき液
CN114702527B (zh) * 2022-03-08 2024-06-04 徐州浩通新材料科技股份有限公司 一种由钯粉制备硫酸乙二胺钯(ⅱ)的方法
CN114773181B (zh) * 2022-03-08 2024-06-11 徐州浩通新材料科技股份有限公司 一种水合双草酸根钯(ⅱ)酸的制备方法

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1771053A1 (de) * 1968-03-28 1971-11-25 Telefunken Patent Verfahren zum stromlosen Abscheiden von Metallschichten der Platinmetallgruppe auf Oberflaechen metallischer und nichtmetallischer Teile

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2915406A (en) * 1958-03-03 1959-12-01 Int Nickel Co Palladium plating by chemical reduction
US3704156A (en) * 1970-07-13 1972-11-28 Du Pont Catalyst solution for electroless plating on nonconductors
US4006047A (en) * 1974-07-22 1977-02-01 Amp Incorporated Catalysts for electroless deposition of metals on comparatively low-temperature polyolefin and polyester substrates

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1771053A1 (de) * 1968-03-28 1971-11-25 Telefunken Patent Verfahren zum stromlosen Abscheiden von Metallschichten der Platinmetallgruppe auf Oberflaechen metallischer und nichtmetallischer Teile

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5882736A (en) * 1993-05-13 1999-03-16 Atotech Deutschland Gmbh palladium layers deposition process
DE102005046351A1 (de) * 2005-09-28 2007-04-05 Knorr-Bremse Systeme für Nutzfahrzeuge GmbH Bremsbelag, insbesondere für eine Scheibenbremse eines Nutzfahrzeugs
US9101915B2 (en) 2012-12-18 2015-08-11 Umicore Ag & Co. Kg Catalyst particles comprising a layered core-shell-shell structure and method of their manufacture
US9440224B2 (en) 2012-12-18 2016-09-13 Umicore Ag & Co. Kg Catalyst particles comprising hollow multilayered base metal-precious metal core/shell particles and method of their manufacture

Also Published As

Publication number Publication date
FR2652822B1 (fr) 1993-06-11
US5085693A (en) 1992-02-04
FR2652822A1 (fr) 1991-04-12
JPH03134178A (ja) 1991-06-07

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