US3672964A - Plating on aluminum,magnesium or zinc - Google Patents

Plating on aluminum,magnesium or zinc Download PDF

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US3672964A
US3672964A US125334A US3672964DA US3672964A US 3672964 A US3672964 A US 3672964A US 125334 A US125334 A US 125334A US 3672964D A US3672964D A US 3672964DA US 3672964 A US3672964 A US 3672964A
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nickel
metal
plating
aluminum
coating
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Harold Edward Bellis
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EIDP Inc
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EI Du Pont de Nemours and Co
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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
    • C23C18/52Chemical 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 using reducing agents for coating with metallic material not provided for in a single one of groups C23C18/32 - C23C18/50
    • 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
    • C23C18/32Coating with nickel, cobalt or mixtures thereof with phosphorus or boron
    • C23C18/34Coating with nickel, cobalt or mixtures thereof with phosphorus or boron using reducing agents

Definitions

  • a process for plating aluminum, magnesium or zinc with an adherent nickel coating comprises contacting the surface of the metal to be treated with an aqueous solution of hydrofluoric acid or a material which releases hydrofluoric acid, such as ammonium bifiuoride, and a.
  • soluble, catalytic metal salt of a metal such as nickel, iron or silver
  • a nickel coating which is stress-free to said treated metal surface, preferably 0.2 to 1 mil in thickness, from an amine borane reductive plating solution maintained at a pH of about 6 to 7 and containing an organic monovalent or divalent sulfur compound.
  • a thicker nickel overcoating can be subsequently applied to the nickel coating using either hypophosphite or borohydride reductive plating baths, or electroplated nickel. Further, adhesion and wear resistance can be upgraded by post heat-treating.
  • This invention relates to processes for plating metals and more particularly to processes for nickel plating aluminum, magnesium, zinc or alloys therebetween.
  • Prior art Aluminum, magnesium and zinc are metals which are relatively soft and require a hard coating to upgrade their wear resistance and corrosion resistance, or a coating to improve their solderability.
  • the metals have been coated with a thin conversion coating such as chromate, which was adequate for metal-to-plastic wear contact but quickly broke down in metal-to-metal wear contact.
  • the claimed invention of the above-mentioned patent involves (1) etching the aluminum with a solution containing nitric acid and, optionally, hydrofluoric acid when the aluminum contains silicon, (2) applying a sodium silicate solution and then baking it on the aluminum, (3) nickel plating the treated aluminum with a hypophosphite electroless nickel plating solution, (4) applying an acidic rinse, and (5) applying an electroplated nickel. It is stated that such a process fills irregularities such as pits and voids which are present in the surface of the aluminum. Such elaborate processes produce nickel plates coated on the aluminum which exhibit only marginal adhesion performance and breakdown in metal-metal wear situations.
  • a process for plating a. metal selected from the group consisting of aluminum, magnesium, zinc and alloys therebetween comprising: contacting the surface of said metal with an aqueous solution containing hydrofluoric acid and a soluble metal salt, the metal of said metal salt being a metal which is displaced by aluminum, magnesium or zinc and which is catalytic to the plating of nickel by chemical reduction, and reductively plating the treated metal surface with a nickel coating from an amine borane reductive plating solution maintained at a pH of about 6 to 7 and containing an organic monovalent or divalent sulfur compound.
  • the present process for nickel plating aluminum, magnesium or zinc employs a specific pretreatment and a specific electroless plating bath to produce a nickel coating which does not delaminate under severe wear service conditions.
  • the metal article to be plated is contacted with an aqueous solution containing hydrofluoric acid, which can be derived from a material which releases hydrofluoric acid such as ammonium bifiuoride or an alkali metal fluoride, and a soluble metal salt, from which the metal of the salt is deposited on the surface of the metal article as a thin, semicontinuous layer which is preferably catalytic to the subsequent electroless nickel step.
  • the temperature of the solution is generally maintained below about 45 C., usually between 25 and 45 C., and preferably between 30 and 40 C. At temperatures much above 45 C.
  • the solution can eat away the article to be plated, leaving the surface pitted and less desirable for the subsequent electroless nickel plating operation; however, higher temperatures can be used if the treating solution is quite dilute and/ or the contact time is quite short.
  • An important consideration in the treatment is that the metal surface roughness will be within the range of 15 to 50 microinches.
  • the concentration of hydrofluoric acid in the aqueous solution is between about 1 and 25 percent by weight of the solution, and preferably will be between about 3 and 15 percent by weight. While the concentration of the metal salt will vary with the amount of hydrofluoric acid present, the upper limit will be the solubility of a particular metal salt in the solution and the lower limit will be the concentration at which pitting of the article to be plated occurs, i.e., the hydrofluoric acid is corroding or pitting the articles surface faster than the metal from the metal salt is being deposited. Generally, the concentration of the metal salt will be between 5 and 50 percent by weight of the solution.
  • the metal salt used in the solution must fulfill three requirements (1) it must be soluble in the hydrofluoric acid solution (2) the metal of the salt must be displaced by aluminum, magnesium or zinc, as the case may be, when the solution is contacted with the metal article to be plated, and (3) the metal as deposited on the surface of the metal article to be plated must present a catalytic surface for the subsequent electroless nickel plating.
  • Preferred salts are metal salts of acids such as the mineral acids and monocarboxylic acids and oxides while the preferred metals of the salts are nickel, iron and silver.
  • other metals which will fulfill the three requirements are aluminum, platinum, brass, manganese, chromium, titanium, molybdenum, tungsten, gold, palladium, cobalt and copper.
  • catalytic surface as used in reductive plating refers to a surface which contains, either in whole or in part, a material which promotes on its surface the reduction of nickel ions.
  • the metal to be plated is treated with the above-described aqueous solution at the desired temperature with or without the application of a cathodic electric current to the part.
  • the time of contact will depend on whether an electric current is applied. Generally, the time should 4 be as short as possible to avoid corroding the surface of from the circles is noted. Results are graded as pass the article but still deposit a layer of metal from the for no delamination, fail for complete delam1nat1on, metal salt. If an electric current is used, the contact time or marginal for some delamination. Coating continuity will be from about 1 to 10 seconds, while about 0.5 to 10 is measured by a 1-hour exposure to boiling l percent minutes will be used if no electric current is applied.
  • the thickness of the nickel coating depends to some One of the nickel plated aluminum sheets was heatextent on subsequent treatments. For example, if the electreated at 200 C. in a forced air oven without damage. troless nickel coating is to be overcoated with electro- The coating adhesion was increased in that a smaller plated nickel or nickel applied from a standard sodium diameter bulge of greater severity was produced before borohydride bath or sodium hypophosphite chemical platdelamination of the coating occurred. ing bath, the thickness should be at least 0.1 mil, prefer- When an approximately 3 inch x 4 inch zinc panel ably from 0.2 to 1 mil. If no overcoat is to be applied, was substituted for the aluminum in Example 1, similar the thickness can be whatever is desired. Generally, howresults were obtained.
  • the coating can be heat-treated at Using the dlmethylamlhe borane p g bath of Exama temperature within the range of about 150 C. to 300 ple l and various aqueous treating solutions, the alumi- C. either after plating or after the nickel overcoat is apnum pieces of Example 1 were treated, plated and the plied. plated pieces tested. The results are shown in Table 11.
  • Example 1 was repeated except other Sulfur Adhesloll 18 measured y the Punch test Whlch 14! Inch pounds were substituted for thiodiglycolic acid with 10 /1 inch h es a e punched in the S e t the Coating essentially equivalent results. These sulfur compounds bulging outward and the extent of coating delamination were mercapto acetic acid, dithiodiglycolic acid, and
  • EXAMPLE 8 Using the baths and procedure of Example 1, an aluminum alpha block used to test wear resistance in the ASTM Test D 2714 using the LFW-l Wear testing device was nickel plated to a thickness of 1.5 mils. The coating after 25,000 cycles had a scar in lubricated wear at 300 lbs. load of 15 mils As a control, an aluminum alpha block was treated with a standard zincate solution (Control 2 in Example 1) and nickel plated in a standard sodium hypophosphite nickel plating bath at 90 C. to a nickel thickness of 1.5 mils. This nickel coating had a scar volume in the lubricated wear test of 1250 mils EXAMPLE 9 Example 1 was repeated to give a nickel coating on the pieces of aluminum 0.2 mil in thickness.
  • a portion of the plated pieces was placed in a standard sodium borohydride nickel plating bath at 92 C. and a portion was placed in a standard sodium hypophosphite nickel plating bath at 90 C. until the coating increased in thickness to 1 mil. Both coatings were adherent and there was no evidence of undercutting of the coatings despite a highly alkaline bath in the case of the sodium borohydride bath.
  • a process for plating nickel by chemical reduction on a metal selected from the group consisting of aluminum, magnesium, zinc and alloys therebetween comprising: contacting the surface of said metal with an aqueous solution containing hydrofluoric acid and a soluble metal salt, the metal of said metal salt being a metal which is displaced by aluminum, magnesium or zinc and which is catalytic to the plating of nickel by chemical reduction, and reductively plating the treated metal surface with a nickel coating from an amine borane reductive plating solution maintained at a pH of about 6 to 7 and containing an organic monovalent or divalent sulfur compound.
  • the temperature for contacting is below about 45 C. and the soluble, metal salt is selected from the group consisting of salts of nickel, copper, iron and silver and is at a concentration in the solution ranging from the point at which hydrofluoric acid dissolves the metal surface faster than the metal from the metal salt is deposited, to the solubility limit of the metal salt in the solution.
  • nickel coating is overcoated with a coating of electroplated nickel, nickel reductively plated from a sodium borohydride plating bath or nickel reductively plated from a sodium hypophosphite plating bath.
  • a process for nickel plating a metal selected from the group consisting of aluminum, magnesium, zinc and alloys therebetween comprising: applying to the surface of said metal an aqueous solution of about 1 to 25 percent by weight hydrofluoric acid and 5 to percent by weight of a nickel salt selected from the group consisting of nickel acetate, nickel oxide and a nickel salt of a mineral acid at a temperature within the range of about 25 to 45 C. and applying a nickel coating about 0.2 to 1 mil in thickness to the metal surface from an amine borane reductive plating solution maintained at a pH of about 6 to 7 and containing an organic monovalent or divalent sulfur compound.

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  • Chemical Kinetics & Catalysis (AREA)
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Abstract

A PROCESS FOR PLATING ALUMINUM, MAGNESIUM OR ZINC WITH AN ADHERENT NICKEL COATING IS PROVIDED. THE PROCESS COMPRISES CONTACTING THE SURFACE OF THE METAL TO BE TREATED WITH AN AQUEOUS SOLUTION OF HYDROFLUORIC ACID OR A MATERIAL WHICH RELEASES HYDROFLUORIC ACID, SUCH AS AMMONIUM BIFLUORIDE, AND A SOLUBLE, CATALYTIC METAL SALT OF A METAL SUCH AS NICKEL, IRON OR SILVER, AND SUBSEQUENTLY APPLYING A NICKEL COATING WHICH IS STRESS-FREE TO SAID TREATED METAL SURFACE, PREFERABLY 0.2 TO 1 MIL IN THICKNESS, FROM AN AMINE BORANE REDUCTIVE PLATING SOLUTION MAINTAINED AT A PH OF ABOUT 6 TO 7 AND CONTAINING AN ORGANIC MONOVALENT OR DIVALENT SULFUR COMPOUND. A THICKER NICKEL OVERCOATING CAN BE SUBSEQUENTLY APPLIED TO THE NICKEL COATING USING EITHER HYPOPHOSPHITE OR BOROHYDRIDE REDUCTIVE PLATING BATHS, OR ELECTROPLATED NICKEL. FURTHER, ADHESION AND WEAR RESISTANCE CAN BE UPGRADED BY POST HEAT-TREATING.

Description

United States Patent 01 fice Patented June 27, 1972 US. Cl. 204-33 10 Claims ABSTRACT OF THE DISCLOSURE A process for plating aluminum, magnesium or zinc with an adherent nickel coating is provided. The process comprises contacting the surface of the metal to be treated with an aqueous solution of hydrofluoric acid or a material which releases hydrofluoric acid, such as ammonium bifiuoride, and a. soluble, catalytic metal salt of a metal such as nickel, iron or silver, and subsequently applying a nickel coating which is stress-free to said treated metal surface, preferably 0.2 to 1 mil in thickness, from an amine borane reductive plating solution maintained at a pH of about 6 to 7 and containing an organic monovalent or divalent sulfur compound. A thicker nickel overcoating can be subsequently applied to the nickel coating using either hypophosphite or borohydride reductive plating baths, or electroplated nickel. Further, adhesion and wear resistance can be upgraded by post heat-treating.
BACKGROUND OF THE INVENTION Field of invention This invention relates to processes for plating metals and more particularly to processes for nickel plating aluminum, magnesium, zinc or alloys therebetween.
Prior art Aluminum, magnesium and zinc are metals which are relatively soft and require a hard coating to upgrade their wear resistance and corrosion resistance, or a coating to improve their solderability. Heretofore, the metals have been coated with a thin conversion coating such as chromate, which was adequate for metal-to-plastic wear contact but quickly broke down in metal-to-metal wear contact.
In US. Pat. 3,472,742, issued Oct. 14, 1969', to the National Aeronautics and Space Administration, the upgrading of aluminum surfaces is described. The prior art at that time is described as treating the aluminum surface with the usual etching bath, electroplating nickel onto the surface and then, to achieve satisfactory adhesion of the nickel to aluminum, the plated aluminum was baked at an elevated temperature as high as 500 C. Variations of this process have been in the etching bath or electroplating bath.
The claimed invention of the above-mentioned patent involves (1) etching the aluminum with a solution containing nitric acid and, optionally, hydrofluoric acid when the aluminum contains silicon, (2) applying a sodium silicate solution and then baking it on the aluminum, (3) nickel plating the treated aluminum with a hypophosphite electroless nickel plating solution, (4) applying an acidic rinse, and (5) applying an electroplated nickel. It is stated that such a process fills irregularities such as pits and voids which are present in the surface of the aluminum. Such elaborate processes produce nickel plates coated on the aluminum which exhibit only marginal adhesion performance and breakdown in metal-metal wear situations.
SUMMARY OF THE INVENTION According to the present invention there is provided a process for plating a. metal selected from the group consisting of aluminum, magnesium, zinc and alloys therebetween comprising: contacting the surface of said metal with an aqueous solution containing hydrofluoric acid and a soluble metal salt, the metal of said metal salt being a metal which is displaced by aluminum, magnesium or zinc and which is catalytic to the plating of nickel by chemical reduction, and reductively plating the treated metal surface with a nickel coating from an amine borane reductive plating solution maintained at a pH of about 6 to 7 and containing an organic monovalent or divalent sulfur compound.
DETAILED DESCRIPTION OF THE INVENTION The present process for nickel plating aluminum, magnesium or zinc employs a specific pretreatment and a specific electroless plating bath to produce a nickel coating which does not delaminate under severe wear service conditions.
Initially, the metal article to be plated is contacted with an aqueous solution containing hydrofluoric acid, which can be derived from a material which releases hydrofluoric acid such as ammonium bifiuoride or an alkali metal fluoride, and a soluble metal salt, from which the metal of the salt is deposited on the surface of the metal article as a thin, semicontinuous layer which is preferably catalytic to the subsequent electroless nickel step. The temperature of the solution is generally maintained below about 45 C., usually between 25 and 45 C., and preferably between 30 and 40 C. At temperatures much above 45 C. the solution can eat away the article to be plated, leaving the surface pitted and less desirable for the subsequent electroless nickel plating operation; however, higher temperatures can be used if the treating solution is quite dilute and/ or the contact time is quite short. An important consideration in the treatment is that the metal surface roughness will be within the range of 15 to 50 microinches.
The concentration of hydrofluoric acid in the aqueous solution is between about 1 and 25 percent by weight of the solution, and preferably will be between about 3 and 15 percent by weight. While the concentration of the metal salt will vary with the amount of hydrofluoric acid present, the upper limit will be the solubility of a particular metal salt in the solution and the lower limit will be the concentration at which pitting of the article to be plated occurs, i.e., the hydrofluoric acid is corroding or pitting the articles surface faster than the metal from the metal salt is being deposited. Generally, the concentration of the metal salt will be between 5 and 50 percent by weight of the solution.
The metal salt used in the solution must fulfill three requirements (1) it must be soluble in the hydrofluoric acid solution (2) the metal of the salt must be displaced by aluminum, magnesium or zinc, as the case may be, when the solution is contacted with the metal article to be plated, and (3) the metal as deposited on the surface of the metal article to be plated must present a catalytic surface for the subsequent electroless nickel plating. Preferred salts are metal salts of acids such as the mineral acids and monocarboxylic acids and oxides while the preferred metals of the salts are nickel, iron and silver. However, other metals which will fulfill the three requirements are aluminum, platinum, brass, manganese, chromium, titanium, molybdenum, tungsten, gold, palladium, cobalt and copper. The term catalytic surface as used in reductive plating refers to a surface which contains, either in whole or in part, a material which promotes on its surface the reduction of nickel ions.
The metal to be plated is treated with the above-described aqueous solution at the desired temperature with or without the application of a cathodic electric current to the part. The time of contact will depend on whether an electric current is applied. Generally, the time should 4 be as short as possible to avoid corroding the surface of from the circles is noted. Results are graded as pass the article but still deposit a layer of metal from the for no delamination, fail for complete delam1nat1on, metal salt. If an electric current is used, the contact time or marginal for some delamination. Coating continuity will be from about 1 to 10 seconds, while about 0.5 to 10 is measured by a 1-hour exposure to boiling l percent minutes will be used if no electric current is applied. In by weight sodium hydroxide which is aggressive to the the latter case, an optimum time is about 1 minute. substrate if the coatingis porous. Results are graded as After treatment with the above-described aqueous sopass for no delamination and fail for complete lution, the treated article is nickel plated from an amine delamination. borane chemical plating bath maintained at a pH of 6 The invention can be further illustrated by referring to 7 which contains an organic monovalent or divalent t0 the following eXamPIeS in Which Parts and Percentages sulfur compound. Such a bath yields a ductile coating are by weight unless otherwise indicated. with low stress, i.e., when the coating is self-supporting, EXAMPLE 1 it is free from distortion caused by tensile or compressive u forces. 'Amine borane plating baths are known to those In thls m the followmg dlmethylamme borane skilled in the art. US. Pat. 3,062,666 issued to Henry G. (DMAB) Platmg bath was used at McLeod on Nov. 6, 1962; US. Pat. 3,338,726 issued to Talivaldis Berzins on Aug. 29, 1967; and US. Pat. Nwlsel acetate 5 2 50 3,234,031 issued to Eberhard Zirngiebl and Heinz Giinter i 25 on Feb. 8, 1966, describe amine borane nickel plating Lactlc acld 25 baths and processes for chemically plating nickel from M F such baths onto catalytic surfaces. The disclosures of Thlodlglyfohc 301d P and uslng ammomum these patents are hereby incorporated by reference. The hydIOXlde Plating bath P is maintained between P 6 and Pieces of aluminum sheeting 20 mils in thickness and a above 7, the metal article tends to dissolve and at a. varying in size up to 2 inches 4 inches were immersed p the nickel coating will d to have stresses in the DMAB plating bath and plated for minutes Whleh W111 cause the eoatlhg t0 delamlhate- The tf to give a coating of 0.1 mil. Prior to plating, a variety levelils eP P the Presence of Sulfur Stablhzef of aqueous treatment solutions based on zincate deposiand Its concentratlon in the bath- Generally, the Sulfur tion were used to remove the aluminum oxide surface. compound is at a concentration of (1001 to 5 and An aqueous solution of the present invention was also a concentration of 0.01 to 1 g./l. is usually SllfilClCllt. USC- 30 used Adhesion and continuity of coating tests were con. ful sulfur compounds are known to those skilled in the ducted as described previously, and the results are shown art. in Table I.
TABLE I Example Treatin solution Temp., Contin- No. (om/gang O. Time Coated Adherent uous Control..- N Yes Fail Fail.
Do--- ZnO (13)-NaOH (70).--- 20 1minute Yes do Do. Do--. ZnSO; (96)-HF (8.5%) 25 do Yes.-." MarginaL. Do. 1 NiClz (30)-HF (3.6%)--- 27 do Yes.-. Pass Pass.
The thickness of the nickel coating depends to some One of the nickel plated aluminum sheets was heatextent on subsequent treatments. For example, if the electreated at 200 C. in a forced air oven without damage. troless nickel coating is to be overcoated with electro- The coating adhesion was increased in that a smaller plated nickel or nickel applied from a standard sodium diameter bulge of greater severity was produced before borohydride bath or sodium hypophosphite chemical platdelamination of the coating occurred. ing bath, the thickness should be at least 0.1 mil, prefer- When an approximately 3 inch x 4 inch zinc panel ably from 0.2 to 1 mil. If no overcoat is to be applied, was substituted for the aluminum in Example 1, similar the thickness can be whatever is desired. Generally, howresults were obtained.
ever, 0.2 to 2 mils will be sufiicient for mostend-use applications. EXAMPLES 2-6 To improve the adhesion, hardness and wear resistance of the nickel coating, the coating can be heat-treated at Using the dlmethylamlhe borane p g bath of Exama temperature within the range of about 150 C. to 300 ple l and various aqueous treating solutions, the alumi- C. either after plating or after the nickel overcoat is apnum pieces of Example 1 were treated, plated and the plied. plated pieces tested. The results are shown in Table 11.
TABLE II Temp., Contin- Example No. Treating solution (oz./gal.) C. Time Coated Adherent uous Control NiClz (30)-oxalic acid (10%) 27 1minute-- Yes Fail Fail.
Do NlC1z(30)-HCI(10%) 27 .-do Yes .do Do. Do NlC12(30)-HC1(10%) NaF (10) 27 --do.--- Yes-.-" MarginaL- Do.
27 do Y P ass. 27 do Do. 27 .do. Do. 2 do- Do. 27 do Yes .-do Do.
Nickel coatings applied to aluminum, magnesium or EXAMPLE 7 zmc articles, as described, are adherenband continuous. Example 1 was repeated except other Sulfur Adhesloll 18 measured y the Punch test Whlch 14! Inch pounds were substituted for thiodiglycolic acid with 10 /1 inch h es a e punched in the S e t the Coating essentially equivalent results. These sulfur compounds bulging outward and the extent of coating delamination were mercapto acetic acid, dithiodiglycolic acid, and
Z-mercaptobenzothiazine. Without sulfur in the bath the coatings were cracked and nonadherent.
EXAMPLE 8 Using the baths and procedure of Example 1, an aluminum alpha block used to test wear resistance in the ASTM Test D 2714 using the LFW-l Wear testing device was nickel plated to a thickness of 1.5 mils. The coating after 25,000 cycles had a scar in lubricated wear at 300 lbs. load of 15 mils As a control, an aluminum alpha block was treated with a standard zincate solution (Control 2 in Example 1) and nickel plated in a standard sodium hypophosphite nickel plating bath at 90 C. to a nickel thickness of 1.5 mils. This nickel coating had a scar volume in the lubricated wear test of 1250 mils EXAMPLE 9 Example 1 was repeated to give a nickel coating on the pieces of aluminum 0.2 mil in thickness. A portion of the plated pieces was placed in a standard sodium borohydride nickel plating bath at 92 C. and a portion was placed in a standard sodium hypophosphite nickel plating bath at 90 C. until the coating increased in thickness to 1 mil. Both coatings were adherent and there was no evidence of undercutting of the coatings despite a highly alkaline bath in the case of the sodium borohydride bath.
What is claimed is:
1. A process for plating nickel by chemical reduction on a metal selected from the group consisting of aluminum, magnesium, zinc and alloys therebetween comprising: contacting the surface of said metal with an aqueous solution containing hydrofluoric acid and a soluble metal salt, the metal of said metal salt being a metal which is displaced by aluminum, magnesium or zinc and which is catalytic to the plating of nickel by chemical reduction, and reductively plating the treated metal surface with a nickel coating from an amine borane reductive plating solution maintained at a pH of about 6 to 7 and containing an organic monovalent or divalent sulfur compound.
2. The process of claim 1 wherein the temperature for contacting is below about 45 C. and the soluble, metal salt is selected from the group consisting of salts of nickel, copper, iron and silver and is at a concentration in the solution ranging from the point at which hydrofluoric acid dissolves the metal surface faster than the metal from the metal salt is deposited, to the solubility limit of the metal salt in the solution.
3. The process of claim 2 wherein the hydrofluoric acid concentration in the solution is from about 1 to percent by weight.
4. The process of claim 3 wherein the metal surface is immersed in the aqueous solution maintained at a temperature of about to C.
5. The process of claim 3 wherein the nickel coating is from about 0.2 to 1 mil in thickness.
6. The process of claim 5 wherein the nickel coating is overcoated with a coating of electroplated nickel, nickel reductively plated from a sodium borohydride plating bath or nickel reductively plated from a sodium hypophosphite plating bath.
7. The process of claim 6 wherein the nickel plated metal is heat-treated at a temperature within the range of about 150 to 300 C.
8. The process of claim 5 wherein the nickel plated metal is heat-treated at a temperature within the range of about 150 to 300 C.
9. A process for nickel plating a metal selected from the group consisting of aluminum, magnesium, zinc and alloys therebetween comprising: applying to the surface of said metal an aqueous solution of about 1 to 25 percent by weight hydrofluoric acid and 5 to percent by weight of a nickel salt selected from the group consisting of nickel acetate, nickel oxide and a nickel salt of a mineral acid at a temperature within the range of about 25 to 45 C. and applying a nickel coating about 0.2 to 1 mil in thickness to the metal surface from an amine borane reductive plating solution maintained at a pH of about 6 to 7 and containing an organic monovalent or divalent sulfur compound.
10. The process of claim 9 wherein the nickel plated metal is heat-treated at a temperature within the range of about to 300 C.
References Cited UNITED STATES PATENTS 2,313,756 3/1943 Loose 204-32 R 2,694,017 11/1954 Reschan et al 11750 2,983,634 5/1961 Budininkas 11750 X FOREIGN PATENTS 701,764 1/1965 Canada 11750 GERALD L. KAPLAN, Primary Examiner US. 01. X.R.
117-50, 71 M; 2,04 32 R, 37 R, 38 B, 38 S
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Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3930081A (en) * 1972-11-06 1975-12-30 Oxy Metal Industries Corp Composition and process for displacement plating of zinc surfaces
US3932685A (en) * 1973-11-09 1976-01-13 Motorola, Inc. Aluminum stabilization process and stabilization solution therefor
US4122215A (en) * 1976-12-27 1978-10-24 Bell Telephone Laboratories, Incorporated Electroless deposition of nickel on a masked aluminum surface
US4149132A (en) * 1976-11-06 1979-04-10 U.S. Philips Corporation Method of manufacturing an electromagnet
US4196061A (en) * 1978-08-21 1980-04-01 Chemray Corporation Direct nickel-plating of aluminum
US4197359A (en) * 1975-10-21 1980-04-08 Rager Edgar A Hub for a disk storage medium
US4235648A (en) * 1979-04-05 1980-11-25 Motorola, Inc. Method for immersion plating very thin films of aluminum
US4282266A (en) * 1980-05-29 1981-08-04 Rca Corporation Method for determining silicon content in layers of aluminum and silicon
US4371430A (en) * 1979-04-27 1983-02-01 Printing Developments, Inc. Electrodeposition of chromium on metal base lithographic sheet
US4416739A (en) * 1980-04-16 1983-11-22 Rolls-Royce Limited Electroplating of titanium and titanium base alloys
US4545867A (en) * 1979-04-27 1985-10-08 Ballarini John A Process for the direct electrodeposition of gray chromium on aluminum base substrates such as aluminum base lithographic sheets
US4552787A (en) * 1984-02-29 1985-11-12 International Business Machines Corporation Deposition of a metal from an electroless plating composition
US4655884A (en) * 1985-08-19 1987-04-07 General Electric Company Nickel plating of refractory metals
US4670312A (en) * 1985-02-07 1987-06-02 John Raymond Method for preparing aluminum for plating
US4687085A (en) * 1982-07-06 1987-08-18 Honda Giken Kogyo Kabushiki Kaisha Centrifugal clutch instantly engageable and disengageable
US4801360A (en) * 1985-06-19 1989-01-31 Stc Plc Surface treatment of aluminum/silicon alloys
WO1998059091A2 (en) * 1997-06-23 1998-12-30 The Metal Arts Company, Inc. Activation bath for electroless nickel plating
US6652730B1 (en) * 1998-12-01 2003-11-25 Studiengesellschaft Kohle Mbh Aluminum organic electrolytes and method for electrolytic coating with aluminum or aluminum-magnesium-alloys
US6669997B2 (en) 2002-03-26 2003-12-30 National Research Council Of Canada Acousto-immersion coating and process for magnesium and its alloy
US20050008788A1 (en) * 2003-06-26 2005-01-13 Joshi Nayan H. Aqueous acidic immersion plating solutions and methods for plating on aluminum and aluminum alloys
EP1857570A2 (en) * 2006-05-19 2007-11-21 Ching Ho Method for forming a nickel-based layered structure on a magnesium alloy substrate, a surface-treated magnesium alloy article made thereform, and a cleaning solution and a surface treatment solution used therefor

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3123826A1 (en) * 1981-06-16 1983-01-05 Robert Bosch Gmbh, 7000 Stuttgart Process for applying a well-adhering, solderable metal layer to rapidly oxidising metals
JPS58187260A (en) * 1982-04-26 1983-11-01 Mitsubishi Electric Corp Solder sticking method to aluminum metal

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3930081A (en) * 1972-11-06 1975-12-30 Oxy Metal Industries Corp Composition and process for displacement plating of zinc surfaces
US3932685A (en) * 1973-11-09 1976-01-13 Motorola, Inc. Aluminum stabilization process and stabilization solution therefor
US4197359A (en) * 1975-10-21 1980-04-08 Rager Edgar A Hub for a disk storage medium
US4149132A (en) * 1976-11-06 1979-04-10 U.S. Philips Corporation Method of manufacturing an electromagnet
US4125648A (en) * 1976-12-27 1978-11-14 Bell Telephone Laboratories, Incorporated Electroless deposition of nickel on aluminum
US4122215A (en) * 1976-12-27 1978-10-24 Bell Telephone Laboratories, Incorporated Electroless deposition of nickel on a masked aluminum surface
US4196061A (en) * 1978-08-21 1980-04-01 Chemray Corporation Direct nickel-plating of aluminum
US4235648A (en) * 1979-04-05 1980-11-25 Motorola, Inc. Method for immersion plating very thin films of aluminum
US4371430A (en) * 1979-04-27 1983-02-01 Printing Developments, Inc. Electrodeposition of chromium on metal base lithographic sheet
US4545867A (en) * 1979-04-27 1985-10-08 Ballarini John A Process for the direct electrodeposition of gray chromium on aluminum base substrates such as aluminum base lithographic sheets
US4416739A (en) * 1980-04-16 1983-11-22 Rolls-Royce Limited Electroplating of titanium and titanium base alloys
US4282266A (en) * 1980-05-29 1981-08-04 Rca Corporation Method for determining silicon content in layers of aluminum and silicon
US4687085A (en) * 1982-07-06 1987-08-18 Honda Giken Kogyo Kabushiki Kaisha Centrifugal clutch instantly engageable and disengageable
US4552787A (en) * 1984-02-29 1985-11-12 International Business Machines Corporation Deposition of a metal from an electroless plating composition
US4670312A (en) * 1985-02-07 1987-06-02 John Raymond Method for preparing aluminum for plating
US4801360A (en) * 1985-06-19 1989-01-31 Stc Plc Surface treatment of aluminum/silicon alloys
US4655884A (en) * 1985-08-19 1987-04-07 General Electric Company Nickel plating of refractory metals
WO1998059091A2 (en) * 1997-06-23 1998-12-30 The Metal Arts Company, Inc. Activation bath for electroless nickel plating
WO1998059091A3 (en) * 1997-06-23 1999-03-25 Metal Arts Company Inc Activation bath for electroless nickel plating
US6652730B1 (en) * 1998-12-01 2003-11-25 Studiengesellschaft Kohle Mbh Aluminum organic electrolytes and method for electrolytic coating with aluminum or aluminum-magnesium-alloys
US6669997B2 (en) 2002-03-26 2003-12-30 National Research Council Of Canada Acousto-immersion coating and process for magnesium and its alloy
US20050008788A1 (en) * 2003-06-26 2005-01-13 Joshi Nayan H. Aqueous acidic immersion plating solutions and methods for plating on aluminum and aluminum alloys
US7407689B2 (en) 2003-06-26 2008-08-05 Atotech Deutschland Gmbh Aqueous acidic immersion plating solutions and methods for plating on aluminum and aluminum alloys
EP1857570A2 (en) * 2006-05-19 2007-11-21 Ching Ho Method for forming a nickel-based layered structure on a magnesium alloy substrate, a surface-treated magnesium alloy article made thereform, and a cleaning solution and a surface treatment solution used therefor
EP1857570A3 (en) * 2006-05-19 2009-06-17 Great Magtech Technology Co., Ltd Method for forming a nickel-based layered structure on a magnesium alloy substrate, a surface-treated magnesium alloy article made thereform, and a cleaning solution and a surface treatment solution used therefor

Also Published As

Publication number Publication date
DE2213161A1 (en) 1972-09-28
CA962538A (en) 1975-02-11
GB1386375A (en) 1975-03-05
DE2213161B2 (en) 1975-09-18

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