Classifications

• • C—CHEMISTRY; METALLURGY
  • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
  • C22C—ALLOYS
  • C22C5/00—Alloys based on noble metals
  • C22C5/06—Alloys based on silver
• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
  • C25D3/00—Electroplating: Baths therefor
  • C25D3/02—Electroplating: Baths therefor from solutions
  • C25D3/56—Electroplating: Baths therefor from solutions of alloys
  • C25D3/64—Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of silver
• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
  • C25D7/00—Electroplating characterised by the article coated
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01R—ELECTRICALLY-CONDUCTIVE CONNECTIONS; STRUCTURAL ASSOCIATIONS OF A PLURALITY OF MUTUALLY-INSULATED ELECTRICAL CONNECTING ELEMENTS; COUPLING DEVICES; CURRENT COLLECTORS
  • H01R13/00—Details of coupling devices of the kinds covered by groups H01R12/70 or H01R24/00 - H01R33/00
  • H01R13/02—Contact members
  • H01R13/03—Contact members characterised by the material, e.g. plating, or coating materials

Definitions

• the present invention is directed to the electrolytic deposition of an alloy containing predominantly silver.
• Other components of the deposited alloy layer are palladium, tellurium and one or more of the metals Ce, Dy, Pb, Bi, Al, Ga, Ge, Fe, In Co, Ni, Cu, Sn, Sb, Rh, Ru, Ir, Pt, Au.
• the present invention also relates to a method for electrolytic deposition of a corresponding layer using a suitable electrolyte. The use of the electrolytically deposited alloy layer is also claimed.
• Electrical contacts are now installed in practically all electrical devices. Their application ranges from simple plug connectors to safety-relevant, demanding switch contacts in the communication sector, for the automotive industry or aerospace technology.
• the contact surfaces require good electrical conductivities, low and long-term stable contact resistance, good corrosion and wear resistance with the lowest possible insertion forces and good resistance to thermal stress.
• plug contacts are often coated with a hard gold alloy layer consisting of gold-cobalt, gold-nickel or gold-iron. These layers have good wear resistance, good solderability, low and long-term contact resistance and good corrosion resistance. Due to the rising gold price, cheaper alternatives are being sought.
• silver-rich silver alloys As a replacement for the hard gold coating, coating with silver-rich silver alloys (hard silver) has proven to be advantageous. Also because of the high electrical conductivity and good oxidation resistance, silver and silver alloys are among the most important contact materials in electrical engineering. Depending on the metal being alloyed, these silver alloy layers have similar layer properties to the hard gold layers or layer combinations used up to now, such as palladium-nickel with gold flash. In addition, the price of silver is relatively low compared to other precious metals, especially hard gold alloys. One limitation for the use of silver is, for example, that the silver is less resistant to corrosion than hard gold in atmospheres containing sulfur and chlorine.
• tarnish layers made of silver sulfide usually do not pose any great danger, since silver sulfide is semiconducting, soft and can usually be easily displaced by the wiping plug-in process with sufficient contact forces.
• tarnish layers made of silver chloride are non-conductive, hard and not easily displaceable. A higher proportion of silver chloride in the tarnish layers leads to problems with the contact properties (literature: Marjorie Myers: OverView of the Use of Silver in Connector Applications; Interconnect & Process Technology, Tyco Electronics Harrisburg, Feb. 2009).
• silver-palladium alloys are e.g. sulfur-resistant if the proportion of palladium is correspondingly high (DE2914880A1).
• Palladium-silver alloys have been used successfully as wrought alloys as contact materials for a long time. In relay switch contacts, 60/40 palladium-silver alloys are preferably used as inlays. These coatings of electrical contact materials based on precious metals are nowadays also preferably produced galvanically. Although the electrochemical deposition of the palladium-silver alloy layers from mostly alkaline electrolytes has already been well investigated, no practical electrolytes have yet been developed. because the deposited palladium-silver alloy layers did not meet the quality and composition requirements.
• DE102013215476B3 describes the electrolytic deposition of an alloy predominantly containing silver.
• Other alloy components are palladium, tellurium or selenium.
• the alloy layers described here have aging effects, particularly at high temperatures, which are reflected in an increased formation of cracks. It is therefore an object of the present invention to present new and temperature-stable alloy layers which can be produced simply by electrolytic deposition and which are superior to the corresponding alloys of the prior art.
• the alloy layers according to the invention should have advantages over the known predominantly silver-containing alloy layers, which furthermore contain palladium and parture as components.
• an electrolytically deposited, predominantly silver-containing silver-palladium alloy layer comprising less than or equal to 20 at% tellurium based on the entire alloy layer, which additionally contains one or more of the metals Ce, Dy, Pb, Bi, Al, Ga, Ge, Fe, In, Co, Ni, Cu, Sn, Sb, Rh, Ru, Ir, Pt, Au, surprisingly achieves the task at hand.
• Such an alloy layer has high corrosion resistance.
• there is an improved temperature stability and a corresponding electrolyte does not lead to crack formation even at high current densities during the electrolytic deposition of the alloy according to the invention (see Table 1).
• silver-palladium alloy layers which contain tellurium and contain tellurium
• AgPdTe alloy electrolytically deposited silver-palladium alloy layers which contain tellurium and contain tellurium
• Silver-palladium alloy layers containing predominantly silver, having less than or equal to 20 at% tellurium, based on the total alloy layer, which were produced electrolytically and additionally one or more of the metals Ce, Dy, Pb, Bi, Al, Ga, Ge, Fe, In, Co , Ni, Cu, Sn, Sb, Rh, Ru, Ir, Pt, Au. have, however, are new to the expert.
• These AgPdTe alloy layers preferably additionally have the metals Ce, Dy, Pb, Bi, In, Sn and / or Fe.
• the metals Bi, Pb, Ce are particularly preferred as additional metals. Bi is particularly preferred in this regard.
• the additional metal or metals should be contained in the AgPdTe alloy layer in an amount of less than or equal to 40 at%. Preferably only one additional metal is present in this amount.
• the amount of the additional metal is particularly preferably 0.1-20 at%, more preferably 0.5-10 at% and very particularly preferably 0.5-5 at%. In some cases, smaller amounts of less than 2 at% are sufficient.
• Silver is the main component of this electrolytically produced alloy.
• the alloys deposited according to the invention have a composition which has approximately 50-95 at% silver (preferably only residues: palladium and tellurium and the additional metals).
• the concentrations of the metals to be deposited in the electrolyte are set within the above-mentioned range so that a silver-rich alloy results.
• the concentration of the metals to be deposited the current density used, the proportion of sulfonic acid used and the amount of tellurium compound added also have an influence on the silver concentration in the deposited alloy.
• An alloy in which the silver has a concentration of more than 60 at%, more preferably between 70-99 at%, more preferably 75-97 at% and very particularly preferably 85-95 at% is preferred.
• the alloy layer according to the invention preferably has 0.1-30 at% palladium. However, sufficient palladium should be available for adequate corrosion resistance. As a rule, alloy layers with 1 to 20 at%, more preferably 2 to 15 at% and most preferably 3 to 12 at% of palladium are suitable.
• Another component of the alloy according to the invention is tellurium. This is preferably present in the alloy in a concentration of 0.1-10 at%, preferably 1-5 at% and very preferably 2-4 at%.
• the alloy layer according to the invention is superior to known electrolytically deposited AgPdTe alloys in terms of abrasion resistance and hardness (measured according to DIN EN ISO 6507-1: 2018).
• the alloy layers according to the claims have a hardness of> 250 Hv, preferably> 260 Hv and very preferably> 270 Hv, depending on the alloy composition.
• the present invention relates to a method for the electrolytic deposition of a silver-palladium alloy layer containing predominantly silver, which contain less than or equal to 20 at% tellurium based on the entire alloy layer.
• the process is characterized in that an aqueous, acidic and cyanide-free electrolyte is used which has the following composition: a) a soluble silver salt, preferably as a sulfonate,
• the electrolyte used according to the invention contains salts of silver, palladium and tellurium and additionally one or more of the metals Ce, Dy, Pb, Bi, Al, Ga, Ge, Fe, In, Co, Ni, Cu, Sn, Sb, Rh , Ru, Ir, Pt, Au also as salt.
• These are preferably salts of the additional metals Ce, Dy, Pb, Bi, In, Sn and / or Fe.
• Particularly preferred as additional metals are those of the group Bi, Pb, Ce in this connection. Bi is particularly preferred in this regard.
• the electrolyte according to the invention is used in an acidic pH range. Optimal results can be achieved with pH values in the electrolyte of ⁇ 2. Those skilled in the art know how to adjust the pH of the electrolyte. This is preferably in the strongly acidic range, more preferably ⁇ 1. Extremely strongly acidic deposition conditions are chosen in an extremely advantageous manner, in which the pH value is below 0.8 and may even reach up to 0.1 in extreme cases up to 0.01. In the optimal case, the pH is around 0.6. There may be fluctuations in the pH of the electrolyte during electrolysis. In a preferred embodiment of the method in question, the person skilled in the art therefore proceeds by checking the pH during the electrolysis and, if necessary, adjusting it to the setpoint.
• the pH can be adjusted according to the expert. However, he will be guided by the idea, as few additional ones as possible Introduce substances into the electrolyte that can negatively influence the deposition of the corresponding alloy.
• the pH is therefore adjusted solely by adding a sulfonic acid.
• the added free sulfonic acid is used in a sufficient concentration of 0.25 - 4.75 mol / l.
• the concentration is preferably 0.5-3 mol / l and very particularly preferably 0.8-2.0 mol / l.
• the sulfonic acid serves on the one hand to establish a corresponding pH value in the electrolyte. On the other hand, their use leads to a further stabilization of the electrolyte according to the invention.
• the upper limit of the sulfonic acid concentration is due to the fact that only silver is deposited if the concentration is too high.
• sulfonic acids known to the person skilled in the art for use in electroplating can be used as sulfonic acid.
• Sulfonic acids selected from the group consisting of ethanesulfonic acid, propanesulfonic acid, benzenesulfonic acid, methanesulfonic acid are preferably used.
• Propanesulfonic acid and methanesulfonic acid are particularly preferred in this connection. Methanesulfonic acid is most preferably used.
• the electrolyte used in the method according to the invention has a specific electrolyte density, which can be selected by the person skilled in the art according to his requirements. At 23 ° C., this is preferably between 1.0 and 1.5. A density of 1.0-1.3 is particularly preferred, most preferably 1.0-1.2. The density was determined gravimetrically.
• the temperature which prevails during the deposition of the alloy according to the invention can be chosen at will by the person skilled in the art. It will be based on a sufficient deposition rate and applicable current density range on the one hand and on the other hand on economic aspects and the stability of the electrolyte. It is advantageous to set a temperature of 30 ° C to 90 ° C in the electrolyte.
• the current density which is established in the electrolyte between the cathode and the anode during the deposition process can be chosen by the person skilled in the art in accordance with the efficiency and quality of the deposition.
• the current density in the electrolyte is advantageously 0.1 to 100 A / dm 2, depending on the application and the type of coating system set. If necessary, the current densities can be increased or decreased by adapting the system parameters such as the structure of the coating cell, flow velocities, anode and cathode ratios, etc.
• Advantageous is a current density from 0.25 to 50 A / dm 2, preferably from 0.5 to 20 A / dm 2 and very particularly preferably 1 - 15 A / dm 2.
• the current density is most preferably 2-12 A / dm 2 .
• a salt of the silver which is soluble in the electrolyte can preferably be used as the silver compound to be added to the electrolyte.
• the salts can very particularly preferably be selected from the group consisting of silver methanesulfonate, silver carbonate, silver sulfate, silver phosphate, silver pyrophosphate, silver nitrate, silver oxide, silver lactate.
• the expert should use the phrase that as little additional substances as possible should be added to the electrolyte.
• the person skilled in the art will therefore very preferably choose the sulfonate, preferably the methanesulfonate, as the silver salt to be added.
• the silver compound is preferably present in the electrolyte in a concentration of 0.01-2.5 mol / l silver, more preferably 0.02-1 mol / l silver and very particularly preferably between 0.05-0.2 mol / l silver .
• the palladium compound to be used is also preferably used as a soluble salt or soluble complex in the electrolyte.
• the palladium compound used here is preferably selected from the group consisting of palladium hydroxide, palladium chloride, palladium sulfate, palladium pyrophosphate, palladium nitrate, palladium phosphate, palladium bromide, palladium P salt (diammonitritopalladium (II); ammoniacal solution), palladium glycinate, palladium acetate, palladium EDA , Tetraamine-Pd hydrogen carbonate.
• the palladium compound is added to the electrolyte in a concentration such that there is sufficient deposition in the alloy layer.
• the palladium compound is preferably used in a concentration of 0.001-0.75 mol / l palladium, most preferably the concentration is 0.01-0.2 mol / l palladium in the electrolyte.
• the tellurium compound which is used in the electrolyte can be chosen accordingly by the person skilled in the art within the desired concentration.
• a preferred concentration range is a concentration between 0.05-80 mmol / l tellurium and very particularly preferably between 0.5 - 40 mmol / l tellurium.
• the compounds with which the electrolyte can be provided are those of the tellurium which have the elements in the oxidation state +4 and +6. Compounds in which the said elements have the oxidation states +4 are particularly preferred. In this context, those selected from the group consisting of tellurites, partial acid, telluric acid and tellurate are very particularly preferred. It is extremely preferred to add the tellurium to the electrolyte in the form of a salt of the partial acid.
• Amino acids are used as complexing agents in the present electrolyte. These are preferably those amino acids which have only alkyl groups in the variable radical.
• the use of amino acids such as alanine, glycine and valine is also preferred.
• the use of glycine and / or alanine is very particularly preferred.
• concentration range specified above the person skilled in the art can freely choose the optimum concentration for the amino acid used. It will be based on the fact that a too small amount of amino acid does not lead to the desired stabilizing effect, while its use in too high concentrations can inhibit the deposition of palladium and other alloy metals. It has therefore proven to be particularly advantageous if the palladium is added to the electrolyte as a corresponding palladium-amino acid complex.
• Soluble or insoluble anodes are just as suitable as the combination of soluble and insoluble anodes. If a soluble anode is used, it is particularly preferred if a silver anode is used.
• the insoluble anodes used are preferably those made from a material selected from the group consisting of platinized titanium, graphite, iridium transition metal mixed oxide and special carbon material (“diamond like carbon” DLC) or combinations of these anodes.
• Platinized titanium or iridium-tantalum mixed oxide are particularly preferably used for carrying out the invention. Others can be found at Cobley, A.J. et al. (The use uf insoluble anodes in Acid Sulphate Copper Electrodeposition Solutions, Trans IMF, 2001, 79 (3), pp. 1 13 and 1 14).
• anionic and nonionic surfactants such as, for example, can also be used as wetting agents in the electrolyte according to the invention
• Polyethylene glycol adducts, fatty alcohol sulfates, alkyl sulfates, alkyl sulfonates, aryl sulfonates, alkylarylsulfonates, heteroarylsulfates, betaines, fluorosurfactants and their salts and derivatives are used (see also: Kanani, N: Galvanotechnik; Hanser Verlag, Kunststoff Vienna, 2000; page 84 ff) .
• the use of a methanesulfonate salt, in particular the potassium salt is preferred.
• the present invention relates to the use of the alloy layer according to the invention in electrical contact materials as an end layer or as an intermediate layer in order to increase the corrosion resistance of the contact materials.
• the preferred embodiments for the alloy layer also apply mutatis mutandis to its use.
• the working area of the electrolyte is significantly expanded. Crack-free deposits can be deposited under the same deposition conditions at significantly higher current densities and with significantly higher layer thicknesses.
• the alloy composition of these layers is stable over a large working area, which is a clear advantage for high-speed deposition.
• the alloy according to the invention shows improved properties with regard to abrasion resistance and hardness. The hardness increases by alloying e.g. 1.5 at% Bi from 250 HV to 300 HV.

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• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
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• Electroplating And Plating Baths Therefor (AREA)
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• 2018
  • 2018-10-22 DE DE102018126174.8A patent/DE102018126174B3/de active Active
• 2019
  • 2019-09-17 TW TW108133378A patent/TW202024401A/zh unknown
  • 2019-10-21 CN CN201980069669.7A patent/CN112888811A/zh active Pending
  • 2019-10-21 KR KR1020217015341A patent/KR20210079351A/ko active Search and Examination
  • 2019-10-21 US US17/272,528 patent/US20210324497A1/en not_active Abandoned
  • 2019-10-21 JP JP2021518469A patent/JP2022504178A/ja active Pending
  • 2019-10-21 WO PCT/EP2019/078475 patent/WO2020083799A1/de unknown
  • 2019-10-21 EP EP19791220.7A patent/EP3870739A1/de active Pending

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