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US3150994A - Chemical plating of metal-boron alloys - Google Patents

Chemical plating of metal-boron alloys Download PDF

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US3150994A
US3150994A US753208A US75320858A US3150994A US 3150994 A US3150994 A US 3150994A US 753208 A US753208 A US 753208A US 75320858 A US75320858 A US 75320858A US 3150994 A US3150994 A US 3150994A
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metal
plating
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borohydride
concentration
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Ralph M Hoke
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Callery Chemical Co
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Callery Chemical Co
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    • C—CHEMISTRY; METALLURGY
    • C23—COATING 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
    • C23C—COATING 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
    • C23C18/00—Chemical 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
    • C23C18/16—Chemical 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
    • C23C18/31—Coating with metals
    • C—CHEMISTRY; METALLURGY
    • C23—COATING 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
    • C23C—COATING 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
    • C23C18/00—Chemical 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
    • C23C18/16—Chemical 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
    • C23C18/31—Coating with metals
    • C23C18/32—Coating with nickel, cobalt or mixtures thereof with phosphorus or boron
    • C23C18/34—Coating with nickel, cobalt or mixtures thereof with phosphorus or boron using reducing agents

Definitions

  • Nickel-boron, cobalt-boron, and ferroboron alloys are known for their superior flowing properties, wear resistance, and hardness.
  • Metal boron alloys, or metal borides are particularly useful as coatings for steel and other metals that do not possess these desirable properties.
  • the metal-boron alloys are also useful as catalysts for a number of chemical reactions, e.g., hydrogenation reactions, Coatings of metal-boron alloys on metallic or non-metallic base materials are particularly desirable as catalysts since a maximum amount of catalytic surface is provided by a minimum amount of the metal-boron alloy.
  • This invention is based on my discovery that certain ammoniacal solutions of a borohydride and soluble nickel, cobalt or iron salts are stable and do not spontaneously react.
  • a material with a catalyticaliy active surface is contacted with this stable solution, a reaction occurs at the surface forming an adherent continuous plate of metal-boron alloy on the surface.
  • the alloy plate itself is catalytically active so that the surface reaction can be continued to form a plate of any desired thickness.
  • any clean metal surface, free of oxide film is catalytically active.
  • Glass and ceramic material also exhibit catalytic activity, but they are much less active than metals.
  • Waxes e.g. paraflinic Waxes, natural fibers, and synthetic organic polymers, e.g. polyethylene and nylon, exhibit essentially no catalytic activity.
  • the solution or plating bath of this invention com prises an aqueous solution containing from about: (1) 0.02 to parts by weight metal ion of the metal boron alloy to be plated, (2) 0.01 to 0.2 part by weight of borohydride ion, and (3) 1.5 to parts by weight of ammonia.
  • the metal ion i.e., iron, cobalt, or nickel ion
  • any soluble metal salt such as nickel sulfate, nickel chloride, nickel acetate, cobaltous sulfate, cobaltous chloride or ferrous sulfate or other suitable soluble salts.
  • ferric chloride may be used, ferrous chloride is preferred as there is higher yield of plate produced per unit weight of borohydride used.
  • the borohydride ion is provided by use of any ionic borohydride, e.g., alkali metal borohydride, alkaline earth borohydride or quaternary ammonium borohydrides.
  • ionic borohydride e.g., alkali metal borohydride, alkaline earth borohydride or quaternary ammonium borohydrides.
  • Sodium and potassium borohydride are now pre ferred as they are widely available at moderate cost.
  • the ammonia serves a dual function in the plating bath. It acts as a sequestering agent of the metal ions and also acts to control the pH of the solution. There must be sufiicient ammonia to provide a pH in excess 3,156,???)4 Patented Sept. 29, 1964 of about 10; if the pH of the solution is below about 10, the solution spontaneously reacts. It is preferable to maintain the pH below about 12 since at higher pH values, the plating reaction is very slow. If the pH of a plating bath is too high for plating at a satisfactory rate, it may be adjusted by the addition of an ammonium salt of a strong acid, e.g. ammonium chloride.
  • the borohydride and metal salt should not both be added to the solution before ammonia is added. If the reactive borohydride and metal salt are mixed in aqueous solution a spontaneous reaction occurs. It is generally preferred to add the borohydride to an ammoniacal solution of the metal salt.
  • the plating baths of this invention have varying degrees of activity.
  • the activity of the bath increases With increasing metal ion concentration and increasing borohydride ion concentration.
  • the ammonia concentration, or pH, is particularly important in determining bath activity; the activity increases with decreasing pH.
  • the plating bath may be used at any temperature between about room temperature and the boiling point of the solution.
  • the activity of the bath increases with increasing temperature.
  • a temperature of about 25 to 40 C. is preferred as the bath is sufficiently active to plate at a good rate, and the temperature is not sufliciently high to require closed vessels to keep ammonia in solution.
  • the object to be plated is immersed in the plating bath and the plating commences.
  • the object may conveniently be suspended by a string or rope made of natural or synthetic fiber, or it may be suspended in a cloth or supported by a wooden or synthetic polymer rack. If a metal piece is used to support the object to be plated, some of the bath will be consumed in plating the support. After the object has been plated, it is removed from the bath and washed with Water to remove the bath solution and permitted to dry.
  • Metal objects to be plated must have clean surfaces free of oxide film.
  • the objects are cleaned by any of the conventional cleaning procedures.
  • the clean metal surface catalyzes the chemical reduction reaction which results in a metal-boron alloy plate on the clean surface.
  • Objects of steel, iron, nickel, cobalt, copper and copper base alloys, aluminum and aluminum base alloys, palladium, and other metals may be plated according to this invention.
  • Glass and ceramic objects to be plated must have clean surfaces free of oil or grease films. They may be cleaned by any of the conventional procedures.
  • the plating solution in a vessel that exposes only non-active surfaces to the bath.
  • Synthetic polymer vessels such as polyethylene, may be used, and vessels lined with non-active material are particularly convenient, e.g. parafiin wax lined, polyethylene lined, or polyvinylidene chloride lined vessels.
  • the plating process is then selective; the plating occurs on the metal, glass or ceramic object immersed in the solution and does not occur on the vessel walls. Glass containers may be used when metals are being plated with plating solutions of moderate activity; although the plating is not entirely selective undesired plating on.
  • the glass container is slight.
  • the chemical plating consumes borohydride and metal ion; and desired concentration or concentration range may be maintained by adding additional borohydrides or metal salts to the plating solution.
  • desired concentration or concentration range may be maintained by adding additional borohydrides or metal salts to the plating solution.
  • by-product salt concentration in the bath; e.g., when the reactive ingredients of the plating solution are sodium borohydride and nickel chloride, the by-product salt is sodium chloride.
  • the by-product salts are not detrimental to the process unless they reach a concentration such that the reactive bath components do not have sutlicient solubility. it is more economical to discard the bath rather than remove the by-product salt.
  • compositions of the solutions are expressed in weight percent of anhydrous reactants.
  • the actual metal salts used were hydrates and the ammonia was added as ammonium hydroxide.
  • EXAMPLE H A clean carbon steel panel was immersed in a plating solution containing 0.13 weight percent NiSO 0.04 wt. percent sodium borohydride, 1.42 wt. percent ammonia and 98.41 Wt. percent Water. The plating solution was contained in a glass vessel. The metal panel was plated with nickel-boron alloy and only a negligible amount of alloy was plated on the container.
  • EXAMPLE III Ferroboron alloy was plated on aluminum and carbon steel panels by immersing the panels for several hours at 18 C. in a plating solution containing 1.78 wt. percent Fe(NH (SO 0.03 wt. percent sodium borohydridc, 12.90 wt. percent ammonia, and 85.29 wt. percent water. Some black precipitate formed in the plating solution.
  • EXAMPLE IV A series of plating reactions were performed in which nickel-boron alloy was plated on carbon steel. The conditions and results are set forth in Table I.
  • the increase in plating rate with increasing temperature is illustrated by runs 1 and 2.
  • the decrease in plating ll rate with increasing ammonia concentration, or pH, is illustrated in runs 2, 3, and 4.
  • EXAMPLE VI A mild steel test panel was immersed in a plating solution containing 1.9 wt. percent NiSO 0.2 wt. percent Naiiii 2.7 wt. percent NH and 95.2 wt. percent water maintained at 18 C. After about 2 hours the plating on the panel had essentially stopped. Additional sodium borohydride in an amount equal to 0.1 percent of the weight of the solution was added, and plating immediately recommenced.
  • EXAMPLE VII A plating solution containing 1.9 wt. percent NiSO 2.9 percent EH 0.2 percent NaBl-L and 96 percent water was made in a glass beaker. After several hours standing at room temperature, a continuous adherent coating of nickel-boron plate formed on the portion of the beaker in contact with the solution.
  • the metal-boron coatings formed by the process of this invention generally appear dark to semi-bright.
  • the plated alloy contains from about 4 to 10 percent boron.
  • An aqueous chemical plating solution containing as essential components (1) anionic borohydride, (2) a compound selected from the group consisting of soluble salts of iron, cobalt nd nickel, and (3) ammonia, the proportions of each component being such that the concentration of borohydride ion is between about 0.01 and 0.2 wt. erccnt, the concentration of metal ion is between about 0.02 to 5 wt. percent, and the concentration of ammonia is between about 1.5 to 25 wt. percent.
  • a method of plating metal-boron alloys on an object selected from the class consisting of metal, glass and ceramic objects which comprises the step of contacting the object to be plated with an aqueous plating solution containing as essential components (1) an ionic borohydride, 2) a compound selected from the group consisting of soluble salts of iron, cobalt and nickel, and (3) ammonia, the proportions of each component being such that the concentration of borohydride ion is between about 0.01 to 0.2 wt. percent, the concentration of metal ion is between about 0.02 to 25 wt. percent, and the concentration of ammonia is between about 1.5 to 25 wt. percent.
  • a method according to claim 5 in which an ammonium salt of a strong acid is added to the solution to maintain the pH of the solution.
  • a method according to claim 2 in which the object to be plated is a metal selected from the group consisting of iron and iron base alloys.
  • concentration of borohydride ion being about 0.03 weight percent
  • concentration of heavy metal ion being about 0.1 Weight percent
  • concentration of ammonia being about 3 weight percent.

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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)

Description

United States Patent 3,1593% CHEMTQAL PLATlNG 0F METAL-BORUN ALLOYS Ralph M. Billie, Fair Qahs, (Ialih, assignor to Gallery tjhernicai Company, Pittsburgh, Pa, a corporation of Pennsylvania No Drawing. Filed Aug. 5, 1958, Ser. No. 753,2ti3 11 fiaims. .(tSl. Ill-13G) This invention relates to a method of chemical plating and more particularly to a method of plating objects with metal-boron alloys.
Nickel-boron, cobalt-boron, and ferroboron alloys are known for their superior flowing properties, wear resistance, and hardness. Metal boron alloys, or metal borides are particularly useful as coatings for steel and other metals that do not possess these desirable properties. The metal-boron alloys are also useful as catalysts for a number of chemical reactions, e.g., hydrogenation reactions, Coatings of metal-boron alloys on metallic or non-metallic base materials are particularly desirable as catalysts since a maximum amount of catalytic surface is provided by a minimum amount of the metal-boron alloy.
It has long been known that alkali metal borohydrides, MBH react spontaneously With aqueous solutions of nickel, cobalt, or iron salts to form precipitates of the corresponding metal borides. Metal-boron coatings on steel objects have previously been made by coating the object with a specially precipitated metal boride and firing the object to form an adherent coating.
This invention is based on my discovery that certain ammoniacal solutions of a borohydride and soluble nickel, cobalt or iron salts are stable and do not spontaneously react. When a material with a catalyticaliy active surface is contacted with this stable solution, a reaction occurs at the surface forming an adherent continuous plate of metal-boron alloy on the surface. The alloy plate itself is catalytically active so that the surface reaction can be continued to form a plate of any desired thickness. I have found that any clean metal surface, free of oxide film, is catalytically active. Glass and ceramic material also exhibit catalytic activity, but they are much less active than metals. Waxes, e.g. paraflinic Waxes, natural fibers, and synthetic organic polymers, e.g. polyethylene and nylon, exhibit essentially no catalytic activity.
The solution or plating bath of this invention com prises an aqueous solution containing from about: (1) 0.02 to parts by weight metal ion of the metal boron alloy to be plated, (2) 0.01 to 0.2 part by weight of borohydride ion, and (3) 1.5 to parts by weight of ammonia.
The metal ion, i.e., iron, cobalt, or nickel ion, is provided by use of any soluble metal salt such as nickel sulfate, nickel chloride, nickel acetate, cobaltous sulfate, cobaltous chloride or ferrous sulfate or other suitable soluble salts. it is preferred to use the metal ion of a lower oxidation so that the borohydride is not consumed in reducing a higher oxidation state ion. For example, although ferric chloride may be used, ferrous chloride is preferred as there is higher yield of plate produced per unit weight of borohydride used.
The borohydride ion is provided by use of any ionic borohydride, e.g., alkali metal borohydride, alkaline earth borohydride or quaternary ammonium borohydrides. Sodium and potassium borohydride are now pre ferred as they are widely available at moderate cost.
The ammonia serves a dual function in the plating bath. It acts as a sequestering agent of the metal ions and also acts to control the pH of the solution. There must be sufiicient ammonia to provide a pH in excess 3,156,???)4 Patented Sept. 29, 1964 of about 10; if the pH of the solution is below about 10, the solution spontaneously reacts. It is preferable to maintain the pH below about 12 since at higher pH values, the plating reaction is very slow. If the pH of a plating bath is too high for plating at a satisfactory rate, it may be adjusted by the addition of an ammonium salt of a strong acid, e.g. ammonium chloride. in preparing the plating baths, the borohydride and metal salt should not both be added to the solution before ammonia is added. If the reactive borohydride and metal salt are mixed in aqueous solution a spontaneous reaction occurs. It is generally preferred to add the borohydride to an ammoniacal solution of the metal salt.
The plating baths of this invention have varying degrees of activity. The more active baths plate more rapidly and are particularly desirable for plating glass and ceramic surfaces. The activity of the bath increases With increasing metal ion concentration and increasing borohydride ion concentration. The ammonia concentration, or pH, is particularly important in determining bath activity; the activity increases with decreasing pH.
The plating bath may be used at any temperature between about room temperature and the boiling point of the solution. The activity of the bath increases with increasing temperature. A temperature of about 25 to 40 C. is preferred as the bath is sufficiently active to plate at a good rate, and the temperature is not sufliciently high to require closed vessels to keep ammonia in solution.
The object to be plated is immersed in the plating bath and the plating commences. The object may conveniently be suspended by a string or rope made of natural or synthetic fiber, or it may be suspended in a cloth or supported by a wooden or synthetic polymer rack. If a metal piece is used to support the object to be plated, some of the bath will be consumed in plating the support. After the object has been plated, it is removed from the bath and washed with Water to remove the bath solution and permitted to dry.
Metal objects to be plated must have clean surfaces free of oxide film. The objects are cleaned by any of the conventional cleaning procedures. The clean metal surface catalyzes the chemical reduction reaction which results in a metal-boron alloy plate on the clean surface. Objects of steel, iron, nickel, cobalt, copper and copper base alloys, aluminum and aluminum base alloys, palladium, and other metals may be plated according to this invention.
Glass and ceramic objects to be plated must have clean surfaces free of oil or grease films. They may be cleaned by any of the conventional procedures.
It is preferred to contain the plating solution in a vessel that exposes only non-active surfaces to the bath. Synthetic polymer vessels, such as polyethylene, may be used, and vessels lined with non-active material are particularly convenient, e.g. parafiin wax lined, polyethylene lined, or polyvinylidene chloride lined vessels. The plating process is then selective; the plating occurs on the metal, glass or ceramic object immersed in the solution and does not occur on the vessel walls. Glass containers may be used when metals are being plated with plating solutions of moderate activity; although the plating is not entirely selective undesired plating on.
the glass container is slight.
When plating has proceeded for several hours, a small amount of metal-boron alloy is precipitated from the solution and collects at the bottom of the vessel. This precipitate is itself catalytically active so that if it is not removed some of the plating solution will be consumed by reaction induced by the precipitate. The precipitate may be removed by filtration.
The chemical plating consumes borohydride and metal ion; and desired concentration or concentration range may be maintained by adding additional borohydrides or metal salts to the plating solution. As the plating proceeds there is a build up of by-product salt concentration in the bath; e.g., when the reactive ingredients of the plating solution are sodium borohydride and nickel chloride, the by-product salt is sodium chloride. The by-product salts are not detrimental to the process unless they reach a concentration such that the reactive bath components do not have sutlicient solubility. it is more economical to discard the bath rather than remove the by-product salt.
The following examples are illustrative of the plating solutions of this invention. The compositions of the solutions are expressed in weight percent of anhydrous reactants. The actual metal salts used were hydrates and the ammonia was added as ammonium hydroxide.
EXAMPLE I A plating solution containing 1.9 wt. percent NiSO4,
O.2'wt. percent NaBl-h, 2.7 wt. percentNH and 95.2 Wt.
bronze, cartridge brass, nickel, lnconel, Monel, cupro 1 nickel, aluminum, and carbon steel were plated with nickelboron alloy by immersing the individual metal strips in aliquots of the plating solution for two hours, at about 18 C. i
EXAMPLE H A clean carbon steel panel was immersed in a plating solution containing 0.13 weight percent NiSO 0.04 wt. percent sodium borohydride, 1.42 wt. percent ammonia and 98.41 Wt. percent Water. The plating solution was contained in a glass vessel. The metal panel was plated with nickel-boron alloy and only a negligible amount of alloy was plated on the container.
EXAMPLE III Ferroboron alloy was plated on aluminum and carbon steel panels by immersing the panels for several hours at 18 C. in a plating solution containing 1.78 wt. percent Fe(NH (SO 0.03 wt. percent sodium borohydridc, 12.90 wt. percent ammonia, and 85.29 wt. percent water. Some black precipitate formed in the plating solution.
EXAMPLE IV EXAMPLE V A series of plating reactions were performed in which nickel-boron alloy was plated on carbon steel. The conditions and results are set forth in Table I.
. Table I PLATING NICKEL-BORON ALLOYS ON MILD STEEL Run N0. 1 2 1 3 4 Plating Composition (wt. percent)- lCl2 2. 62 2. 62 2. 62 1. 80 NaBH4 0. l5 0. 45 0. 45 0.22 NH 17. 17. 20 13. 90 3. 32 E 0. 79. 73 79. 73 83. 03 94. 46
Temperature (deg.) 22. 50 40 40 Plating Time (min) 213 213 52 108 Average Plating Rate (in X10- /hr. 0. 0027 0. 006 0.016 0. 029
The increase in plating rate with increasing temperature is illustrated by runs 1 and 2. The decrease in plating ll rate with increasing ammonia concentration, or pH, is illustrated in runs 2, 3, and 4.
EXAMPLE VI A mild steel test panel was immersed in a plating solution containing 1.9 wt. percent NiSO 0.2 wt. percent Naiiii 2.7 wt. percent NH and 95.2 wt. percent water maintained at 18 C. After about 2 hours the plating on the panel had essentially stopped. Additional sodium borohydride in an amount equal to 0.1 percent of the weight of the solution was added, and plating immediately recommenced.
EXAMPLE VII A plating solution containing 1.9 wt. percent NiSO 2.9 percent EH 0.2 percent NaBl-L and 96 percent water was made in a glass beaker. After several hours standing at room temperature, a continuous adherent coating of nickel-boron plate formed on the portion of the beaker in contact with the solution.
The metal-boron coatings formed by the process of this invention generally appear dark to semi-bright. The plated alloy contains from about 4 to 10 percent boron.
According to the provisions of the patent statutes, I have explained the principle and mode of practicing my invention, have described what I now consider to be its best embodiments. However, I desire to have it understood that within the scope of the appended claims, the
invention may be practiced otherwise than as specifically described.
I claim:
1. An aqueous chemical plating solution containing as essential components (1) anionic borohydride, (2) a compound selected from the group consisting of soluble salts of iron, cobalt nd nickel, and (3) ammonia, the proportions of each component being such that the concentration of borohydride ion is between about 0.01 and 0.2 wt. erccnt, the concentration of metal ion is between about 0.02 to 5 wt. percent, and the concentration of ammonia is between about 1.5 to 25 wt. percent.
2. A method of plating metal-boron alloys on an object selected from the class consisting of metal, glass and ceramic objects which comprises the step of contacting the object to be plated with an aqueous plating solution containing as essential components (1) an ionic borohydride, 2) a compound selected from the group consisting of soluble salts of iron, cobalt and nickel, and (3) ammonia, the proportions of each component being such that the concentration of borohydride ion is between about 0.01 to 0.2 wt. percent, the concentration of metal ion is between about 0.02 to 25 wt. percent, and the concentration of ammonia is between about 1.5 to 25 wt. percent.
3. A method according to claim 2 in which the borohydride is sodium borohydride.
4. A method according to claim 2 in which the plating solution is maintained at a temperature between about 25 C. and 40 C.
5. A method according to claim 2 in which the pH of the plating solution is maintained between about 10 and 12.
6. A method according to claim 5 in which an ammonium salt of a strong acid is added to the solution to maintain the pH of the solution.
7. A method according to claim 2 in which the concentration of borohydride ion is maintained by the periodic addition of an ionic borohyd'ride.
8. A method according to claim 2 in which the concentration'of metal ion is maintained by the periodic addition of a soluble metal salt. 7
9. A method according to claim 2 in which the object to be plated is a metal selected from the group consisting of iron and iron base alloys.
10. A method of plating metal-boron alloys on an object selected from the class consisting of metal, glass and ceramic objects which comprise the step of contacting the objects which comprises the step of contacting the metal 10 object to be plated with an aqueous plating solution containing as essential components (1) an ionic borohydride, (2) a compound selected from the group consisting of soluble salts of a heavy metal, and (3) ammonia, the
concentration of borohydride ion being about 0.03 weight percent, the concentration of heavy metal ion being about 0.1 Weight percent and the concentration of ammonia being about 3 weight percent.
References Cited in the file of this patent UNITED STATES PATENTS 2,461,661 Schlesinger Feb. 15, 194.9 2,726,170 Warf Dec. 6, 1955 OTHER REFERENCES Hard: Chemistry of the Hydrides, 1952, John Wiley and Sons, p. 84.

Claims (1)

1. AN AQUEOUS CHEMICAL PLATING SOLUTION CONTAINING AS ESSENTIAL COMPONENTS (1) AT IONIC BOROHYDRIDE, (2) A COMPOUND SELECTED FROM THE GROUP CONSISTING OF SOLUBLE SALTS OF IRON, COBALT AND NICKEL, AND (3) AMMONIA, THE PROPORTIONS OF EACH COMPONENT BEING SUCH THAT THE CONCENTRATION OF BOROHYDRIDE ION IS BETWEEN ABOUT 0.01 AND 0.2 WT. PERCENT, THE CONCENTRATION OF METAL ION IS BETWEEN ABOUT 0.02 TO 5 WT. PERCENT, AND THE CONCENTRATION OF AMMONIA IS BETWEEN ABOUT 1.5 TO 25 WT. PERCENT.
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3373054A (en) * 1963-07-22 1968-03-12 Bayer Ag Chemical plating
US3539390A (en) * 1966-08-26 1970-11-10 Bosch Gmbh Robert Process for making a semiconductor device
FR2472952A1 (en) * 1980-01-02 1981-07-10 Ceskoslovenska Akademie Ved NICKEL BASED CATALYST FIXED ON A SUPPORT AND USE OF THE CATALYST IN A HYDROGENATION PROCESS OF POLYUNSATURATED ORGANIC COMPOUNDS TO THE PARTIALLY OR COMPLETELY SATURATED COMPOUNDS
US4515870A (en) * 1981-07-22 1985-05-07 Allied Corporation Homogeneous, ductile iron based hardfacing foils
US4576873A (en) * 1981-07-22 1986-03-18 Allied Corporation Homogeneous, ductile iron based hardfacing foils
US4983428A (en) * 1988-06-09 1991-01-08 United Technologies Corporation Ethylenethiourea wear resistant electroless nickel-boron coating compositions
US5017410A (en) * 1988-05-23 1991-05-21 United Technologies Corporation Wear resistant electroless nickel-boron coating compositions
US6183546B1 (en) 1998-11-02 2001-02-06 Mccomas Industries International Coating compositions containing nickel and boron
US10096547B2 (en) 1999-10-02 2018-10-09 Uri Cohen Metallic interconnects products

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2461661A (en) * 1945-01-09 1949-02-15 Hermann I Schlesinger Preparation of alkali metal compounds
US2726170A (en) * 1954-09-07 1955-12-06 Superweld Corp Method of coating steel with nickel-boron

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2461661A (en) * 1945-01-09 1949-02-15 Hermann I Schlesinger Preparation of alkali metal compounds
US2726170A (en) * 1954-09-07 1955-12-06 Superweld Corp Method of coating steel with nickel-boron

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3373054A (en) * 1963-07-22 1968-03-12 Bayer Ag Chemical plating
US3539390A (en) * 1966-08-26 1970-11-10 Bosch Gmbh Robert Process for making a semiconductor device
FR2472952A1 (en) * 1980-01-02 1981-07-10 Ceskoslovenska Akademie Ved NICKEL BASED CATALYST FIXED ON A SUPPORT AND USE OF THE CATALYST IN A HYDROGENATION PROCESS OF POLYUNSATURATED ORGANIC COMPOUNDS TO THE PARTIALLY OR COMPLETELY SATURATED COMPOUNDS
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