US3438798A - Electroless plating process - Google Patents

Electroless plating process Download PDF

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US3438798A
US3438798A US481944A US3438798DA US3438798A US 3438798 A US3438798 A US 3438798A US 481944 A US481944 A US 481944A US 3438798D A US3438798D A US 3438798DA US 3438798 A US3438798 A US 3438798A
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bath
plating
plated
transition metal
nickel
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Donald W Baudrand
Glenn O Mallory Jr
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Arp Inc
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31Coating with metals
    • C23C18/32Coating 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
    • C23C18/36Coating with nickel, cobalt or mixtures thereof with phosphorus or boron using reducing agents using hypophosphites
    • 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

Definitions

  • the process provides for the sensitizing of the material to be plated and thereafter immersing the sensitized material in a plating bath comprising an aqueous solution of a transition metal salt, a transition metal reducing agent, a ligand complexing agent, and a carbonate buffering agent wherein the bath is maintained at a pH in the range of 7 to ll.
  • the material to be plated is left in the bath until plating to the desired depth has been accomplished and the plated material is thereafter removed.
  • This invention relates to electroless transition metal plating and in particular to a process for plating plastics and other materials in a low temperature plating bath.
  • Electroless transition metal plating relates to the autocatalytic deposition of a transition metal such as nickel, cobalt and iron on a catalytic surface.
  • Materials which are catalytic to such plating baths include iron, cobalt, nickel, palladium, gold, aluminum and platinum.
  • Other elements which have to be pretreated to render them catalytic include copper and silver.
  • the materials used with these baths have been metals which do not deform or lose their shape at the operating temperature of such plating baths.
  • a non-catalytic material such as plastic.
  • plastic materials there are many uses in the automotive industry for metal plated plastics.
  • Plating baths heretofore developed for such materials have generally re quired a temperature of at least 150 F. in order to produce plating at a practical rate. Below this temperature these baths are either incapable of plating or plate at such a low rate that their use on a production basis is not feasible.
  • non-conductive materials are frequently sensitive to heat and will deform if placed in a bath that has a temperature above 150 F., the processes have been limited to use with plastics having a high temperature deformation point.
  • plastic materials which could not be plated include A.B.S. (acrylonitrile-butadiene-styrene) and polyesters. Such materials cannot endure temperatures in excess of 140 F. without being subject to serious deformation. Because these specific plastics are widely used in such applications as decorative stripping and on radios, heaters, etc. in automobiles, it is desirable that a method be found for plating transition metals, especially nickel on them.
  • the present invention provides a process which produces plating at a rate comparable to presently known baths.
  • the process is operable at a relatively low temperature and hence is suitable for use in the plating of plastics and other non-conductive materials where a low temperature bath is a prime requisite.
  • the process com- See prises the steps of sensitizing the material to be plated such that it is rendered catalytic to a transition metal plating bath, thereafter immersing the sensitized material in an electroless transition metal plating bath which has been raised to a temperature not in excess of the deformation point of the material, allowing the sensitized material to remain in the bath until plating in the desired thickness has been obtained thereon, and thereafter removing the plated material from the bath.
  • the process of this invention utilizes the electroless bath for plating transition metals such as nickel, cobalt and iron which is described in copending application Ser. No. 479,346 filed Aug. 12, 1965, and now abandoned. Utilization of the plating bath described therein is preferred because such a bath will plate at low temperatures. Where the material to be plated does not deform at low temperatures, the process is also suited for use with conventional electroless transition metal plating baths. By utilizing the baths disclosed in the application just referred to and limiting the operation of the bath to a temperature not in excess of F., the bath of that disclosure produces plating on plastics and other low temperature materials at a satisfactory rate.
  • transition metals such as nickel, cobalt and iron
  • the bath comprises an aqueous solution of a transition metal salt, a ligand complexing agent, a transition metal reducing agent and a carbonate buffering agent wherein the pH of the bath is adjusted by the buffering agent to a value in the range from about 7 to about 11.
  • the first step of the process includes sensitization of the material to be plated prior to immersion in the plating bath.
  • Sensitization relates to the step or steps for making a non-conductive, non-catalytic material catalytic to an electroless plating bath.
  • the result of sensitization is to provide a deposit of a catalytic material over the surface of the non-catalytic material to be plated in Sllfi'lClCIlt quantities to successfully catalyze the plating reaction once the material is introduced into the electroless plating bath.
  • the sensitizing step includes the following.
  • the material to be plated is cleaned to insure that soil, fingerprints, and surface contamination due to handling and storage are completely removed.
  • Non-silicated alkaline-type cleaners are especially suitable for the cleaning operation.
  • plastic is the material to be treated, a highly chelated cleaner is preferable. Thorough cleaning of the material to be plated is a prerequisite for satisfactory etching.
  • a suitable etching solution comprises a concentrated solution of chromic acid having a specific gravity in the range of from 1.6 to 1.68.
  • Other etching baths such as those described in Metallizing of Plastics, Harold Narcus, Reinhold Publishing Co., 1960, are also suitable.
  • the cleaned object is placed in the etching solution and allowed to remain for approximately 5 to 10 minutes.
  • concentration of the etching solution and the length of etching immersion are chosen such that etching is uniform but not severe enough to degrade the material to be plated. Air or mechanical agitation of the etching solution is helpful in preventing stratification of the constitucuts of the etching solution and insuring uniform etching.
  • the amount of catalytic material that can be adsorbed into the surface is dependent on the quality of the etching.
  • An etching operation according to the preceding steps produces a finely abrasive surface which is readily wetted and suitable for trapping and holding a suflicient amount I of fine particles of palladium or other catalytic element.
  • the object When etched, the object is removed and rinsed thoroughly. Proper rinsing is important in order to remove all traces of the etching material from the object surface so as to not contaminate the sensitizing and plating baths. Contamination, particularly of the plating bath, is undesirable because the stability of such plating baths is frequently adversely affected by such a condition.
  • the etched material is immersed in a first sensitizing bath comprising an acidic solution of stannous chloride.
  • Sensitizing bath stabilizing agents such as resorcinol and other reducing agents mentioned in Metallizing of Plastics, previously referred to, are normally added to the stannous chloride bath. The stabilizing agent aids the bath in preventing the tendency of the stannous chloride to oxidize to stannic chloride. Immersion in this first sensitizing bath produces a dispersion of stannous chloride on the surface of the object.
  • the part is then removed from the first sensitizing bath, rinsed and immersed in a second sensitizing solution which comprises a dilute acid solution of palladium chloride.
  • a second sensitizing solution which comprises a dilute acid solution of palladium chloride.
  • Typical formulations for this solution are also described in the publication Metallizing of Plastics previously referred to.
  • a suitable bath comprises an aqueous solution of a transition metal salt, a ligand complexing agent, a transition metal reducing agent, and a carbonaate buffering agent.
  • Typical formulations for such a bath are:
  • Element Preferred Range (grams/liter) (grams/liter) Nickel added as nickel chloride 15.0 5-50 Sodium glycolate 23.0 -100 Glycine 8.0 -30 Sodium hypophosp 25.0 5-50 Sodium carbonate.-.” 30. 0 -60 pH 8.2 7-11 BATH NO. 2
  • Element Preferred Range (grams/liter) (grams/liter) Cobalt added as cobalt chloride 30.0 5-60 Carboxypimelic acid 50. 0 10-100 Glycine 10. 0 5-30 Choline carbonate- 30. 0 10-60 Sodium hypophosphite 30.0 5-100 pH s. 5 7-11
  • Other suitable electroless plating baths comprise an aqueous solution of a transition metal-organic coordination compound, a ligand complexing agent, a transition metal reducing agent and a carbonate buffering agent. Examples of such formulations include:
  • Baths having the general formulations outlined above will plate at a temperature of approximately 60 F. To obtain plating on most plastic and other non-conductive materials, it is sufiicient to maintain the bath at a temperature not in excess of F. Provided the object to be plated remains sufiiciently rigid in baths at temperatures above 120 F. the process of this invention can also be performed with electroless baths whose effective plating temperature is in excess of 120 F.
  • the sensitized object is left in the bath until plating in the desired thickness has been obtained.
  • the object When the object has been immersed in the bath for the length of time necessary to produce the desired plating thickness, it is then removed. After rinsing, the object is ready for electroplating or other desired finishing operations preparatory to use as a finished product.
  • a process for plating transition metals on nonconductive materials comprising the steps of:
  • an electroless transition metal plating bath comprising an aqueous solution of a transition metal organic compound, a ligand complexing agent, a transition metal reducing agent and a carbonate buffering agent wherein the pH of the bath is maintained at a value in the range from about 7 to 11,
  • a process for plating transition metals on non-conductive materials comprising the steps of:
  • an electroless transition metal plating bath comprising an aqueous solution of a transition metal organic coordination corn-pound, a ligand complexing agent, a transition metal reducing agent, and a carbonate buffering agent wherein the pH of the bath is maintained at a value in the range of from about 7 to about 11,
  • a process for plating transition metals on nonconductive materials comprising the steps of:
  • an electroless transition metal plating bath comprising an aqueous solution of a nickel-organic compound, a ligand complexing agent for diminishing competition from ions other than reducing and complexing anions for coordination positions of the nickel, a nickel reducing agent, and a carbonate buffering agent wherein the pH of the bath is maintained within the range of from about 7 to 11,
  • a process for plating transition metals on nonconductive materials comprising the steps of:
  • an electroless transition metal plating bath comprising an aqueous solution of a nickel-organic coordination compound, a ligand complexing agent selected from the class consisting of glycine, citric acid, carboxypemitic acid, cyanoacetic acid, glycolic acid, propionic acid, formic acid, and salts thereof, a hypophosphite reducing agent, and a carbonate buffering agent wherein the pH of the bath is maintained within the range of from about 7 to about 11,
  • a process according to claim 4 wherein the step of depositing a dispersion of a catalytic material on the etched surface comprises the steps of:
  • step of etching the surface of the material to be plated comprises placing the material in a chromic acid solution having a specific gravity in the range of 1.6 to 1.68, wherein the step of immersing the etched material in a first sensitizing bath comprises immersing the material in a stannous chloride solution to produce a pre-sensitizing stannous chloride deposit on the etched surface, and wherein the step of immersing the material in a second sensitizing bath comprises immersing the pre-sensitized material in a palladium chloride solution to produce a dispersion of metallic palladium on the etched surface.
  • a process for plating nickel on non-conductive materials comprising the steps of:
  • preparing a nickel plating bath by preparing an aqueous solution of nickel glycolate in the range of 1 to 30 grams/liter to which is added glycine in the range of 1 to 50 grams/liter, a nickel reducing agent in the range of 1 to 100 grams/liter, and a carbonate buffering agent in the range of 10 to grams/ liter wherein the pH of the bath is maintained within the range of from about 7 to about 11,
  • a process for plating nickel on non-conductive materials comprising the steps of:
  • preparing a nickel plating bath by preparing an aqueous solution of nickel acetate in the range of l to 30 grams/ liter to which is added carboxypimelic acid in the range of 1 to 50 grams/liter, a nickel reducing agent in the range of 1 to grams/liter, and a carbonate buffering agent in the range of 10 to 60 grams/liter wherein the pH of the bath is maintained within a range of from about 7 to about 1 1,

Description

United States Patent l 3,438,798 ELECTROLESS PLATING PROCESS Donald W. Baudrand, Temple City, and Glenn 0. Mailory, .lr., Los Angeles, Calif, assignor, by direct and mesne assignments, to ARE, llnc., a corporation of Maryland No Drawing. Filed Aug. 23, 1965, Ser. No. 481,944 Int. Cl. C23c 17/00; B44d 1/44 US. UL 117-47 8 Claims ABSTRACT OF THE DISCLOSURE A process for plating non-conductive materials such as plastics by means of an electroless transition metal plating bath at a temperature below the deformation temperature of the non-conductive material to be plated. The process provides for the sensitizing of the material to be plated and thereafter immersing the sensitized material in a plating bath comprising an aqueous solution of a transition metal salt, a transition metal reducing agent, a ligand complexing agent, and a carbonate buffering agent wherein the bath is maintained at a pH in the range of 7 to ll. The material to be plated is left in the bath until plating to the desired depth has been accomplished and the plated material is thereafter removed.
This invention relates to electroless transition metal plating and in particular to a process for plating plastics and other materials in a low temperature plating bath.
Electroless transition metal plating relates to the autocatalytic deposition of a transition metal such as nickel, cobalt and iron on a catalytic surface. Materials which are catalytic to such plating baths include iron, cobalt, nickel, palladium, gold, aluminum and platinum. Other elements which have to be pretreated to render them catalytic include copper and silver. In general the materials used with these baths have been metals which do not deform or lose their shape at the operating temperature of such plating baths.
In various instances, it is desirable to be able to plate a non-catalytic material such as plastic. For example, there are many uses in the automotive industry for metal plated plastics. To this end there has been developed processes utilizing plating baths which are suitable for plating on plastic materials and other non-conductors. Plating baths heretofore developed for such materials have generally re quired a temperature of at least 150 F. in order to produce plating at a practical rate. Below this temperature these baths are either incapable of plating or plate at such a low rate that their use on a production basis is not feasible. However, because such non-conductive materials are frequently sensitive to heat and will deform if placed in a bath that has a temperature above 150 F., the processes have been limited to use with plastics having a high temperature deformation point.
Specific examples of plastic materials which could not be plated include A.B.S. (acrylonitrile-butadiene-styrene) and polyesters. Such materials cannot endure temperatures in excess of 140 F. without being subject to serious deformation. Because these specific plastics are widely used in such applications as decorative stripping and on radios, heaters, etc. in automobiles, it is desirable that a method be found for plating transition metals, especially nickel on them.
The present invention provides a process which produces plating at a rate comparable to presently known baths. At the same time, the process is operable at a relatively low temperature and hence is suitable for use in the plating of plastics and other non-conductive materials where a low temperature bath is a prime requisite. The process com- See prises the steps of sensitizing the material to be plated such that it is rendered catalytic to a transition metal plating bath, thereafter immersing the sensitized material in an electroless transition metal plating bath which has been raised to a temperature not in excess of the deformation point of the material, allowing the sensitized material to remain in the bath until plating in the desired thickness has been obtained thereon, and thereafter removing the plated material from the bath.
In its preferred embodiment, the process of this invention utilizes the electroless bath for plating transition metals such as nickel, cobalt and iron which is described in copending application Ser. No. 479,346 filed Aug. 12, 1965, and now abandoned. Utilization of the plating bath described therein is preferred because such a bath will plate at low temperatures. Where the material to be plated does not deform at low temperatures, the process is also suited for use with conventional electroless transition metal plating baths. By utilizing the baths disclosed in the application just referred to and limiting the operation of the bath to a temperature not in excess of F., the bath of that disclosure produces plating on plastics and other low temperature materials at a satisfactory rate. As disclosed in that application, the bath comprises an aqueous solution of a transition metal salt, a ligand complexing agent, a transition metal reducing agent and a carbonate buffering agent wherein the pH of the bath is adjusted by the buffering agent to a value in the range from about 7 to about 11.
The process of this invention will be more readily understood after reference to the following detailed description.
The first step of the process includes sensitization of the material to be plated prior to immersion in the plating bath. Sensitization relates to the step or steps for making a non-conductive, non-catalytic material catalytic to an electroless plating bath. The result of sensitization is to provide a deposit of a catalytic material over the surface of the non-catalytic material to be plated in Sllfi'lClCIlt quantities to successfully catalyze the plating reaction once the material is introduced into the electroless plating bath.
In detail, the sensitizing step includes the following. The material to be plated is cleaned to insure that soil, fingerprints, and surface contamination due to handling and storage are completely removed. Non-silicated alkaline-type cleaners are especially suitable for the cleaning operation. Where plastic is the material to be treated, a highly chelated cleaner is preferable. Thorough cleaning of the material to be plated is a prerequisite for satisfactory etching.
After cleaning, the part is rinsed thoroughly and subjected to an etching solution. A suitable etching solution comprises a concentrated solution of chromic acid having a specific gravity in the range of from 1.6 to 1.68. Other etching baths such as those described in Metallizing of Plastics, Harold Narcus, Reinhold Publishing Co., 1960, are also suitable.
The cleaned object is placed in the etching solution and allowed to remain for approximately 5 to 10 minutes. The concentration of the etching solution and the length of etching immersion are chosen such that etching is uniform but not severe enough to degrade the material to be plated. Air or mechanical agitation of the etching solution is helpful in preventing stratification of the constitucuts of the etching solution and insuring uniform etching. The amount of catalytic material that can be adsorbed into the surface is dependent on the quality of the etching. An etching operation according to the preceding steps produces a finely abrasive surface which is readily wetted and suitable for trapping and holding a suflicient amount I of fine particles of palladium or other catalytic element.
When etched, the object is removed and rinsed thoroughly. Proper rinsing is important in order to remove all traces of the etching material from the object surface so as to not contaminate the sensitizing and plating baths. Contamination, particularly of the plating bath, is undesirable because the stability of such plating baths is frequently adversely affected by such a condition.
After rinsing, the etched material is immersed in a first sensitizing bath comprising an acidic solution of stannous chloride. Sensitizing bath stabilizing agents such as resorcinol and other reducing agents mentioned in Metallizing of Plastics, previously referred to, are normally added to the stannous chloride bath. The stabilizing agent aids the bath in preventing the tendency of the stannous chloride to oxidize to stannic chloride. Immersion in this first sensitizing bath produces a dispersion of stannous chloride on the surface of the object.
The part is then removed from the first sensitizing bath, rinsed and immersed in a second sensitizing solution which comprises a dilute acid solution of palladium chloride. Typical formulations for this solution are also described in the publication Metallizing of Plastics previously referred to. When the stannous chloride-coated object is introduced into the second sensitizer solution, the palladium chloride is reduced to elemental palladium and displaces the dispersion of stannous chloride on the surface of the etched material leaving a dispersion of metallic palladium. The object is now sensitized and capable of catalyzing an electroless plating reaction.
Upon rinsing, the material to be plated is ready for immersion in an electroless plating bath. For plating at a temperature below 120 F. a suitable bath comprises an aqueous solution of a transition metal salt, a ligand complexing agent, a transition metal reducing agent, and a carbonaate buffering agent. Typical formulations for such a bath are:
BATH NO. 1
Element Preferred Range (grams/liter) (grams/liter) Nickel added as nickel chloride 15.0 5-50 Sodium glycolate 23.0 -100 Glycine 8.0 -30 Sodium hypophosp 25.0 5-50 Sodium carbonate.-." 30. 0 -60 pH 8.2 7-11 BATH NO. 2
Element Preferred Range (grams/liter) (grams/liter) BATH N0. 3
Element Preferred Range (grams/liter) (grams/liter) Cobalt added as cobalt chloride 30.0 5-60 Carboxypimelic acid 50. 0 10-100 Glycine 10. 0 5-30 Choline carbonate- 30. 0 10-60 Sodium hypophosphite 30.0 5-100 pH s. 5 7-11 Other suitable electroless plating baths comprise an aqueous solution of a transition metal-organic coordination compound, a ligand complexing agent, a transition metal reducing agent and a carbonate buffering agent. Examples of such formulations include:
Baths having the general formulations outlined above will plate at a temperature of approximately 60 F. To obtain plating on most plastic and other non-conductive materials, it is sufiicient to maintain the bath at a temperature not in excess of F. Provided the object to be plated remains sufiiciently rigid in baths at temperatures above 120 F. the process of this invention can also be performed with electroless baths whose effective plating temperature is in excess of 120 F.
The sensitized object is left in the bath until plating in the desired thickness has been obtained. When the object has been immersed in the bath for the length of time necessary to produce the desired plating thickness, it is then removed. After rinsing, the object is ready for electroplating or other desired finishing operations preparatory to use as a finished product.
What is claimed is:
1. A process for plating transition metals on nonconductive materials comprising the steps of:
(l) sensitizing the surface of the material to be plated such that it is catalytic to an electroless transition metal plating bath,
(2) immersing the sensitized material to be plated in an electroless transition metal plating bath comprising an aqueous solution of a transition metal organic compound, a ligand complexing agent, a transition metal reducing agent and a carbonate buffering agent wherein the pH of the bath is maintained at a value in the range from about 7 to 11,
(3) maintaining the bath at a temperature below the deformation temperature of the material to be plated,
(4) allowing the material to be plated to remain in bath until plating in the desired thickness has been achieved, and
(5) removing the plated material from the bath.
2. A process for plating transition metals on non-conductive materials comprising the steps of:
(1) sensitizing the surface of the material to be plated such that it is catalytic to an electroless transition metal plating bath,
(2) immersing the sensitized material to be plated in an electroless transition metal plating bath comprising an aqueous solution of a transition metal organic coordination corn-pound, a ligand complexing agent, a transition metal reducing agent, and a carbonate buffering agent wherein the pH of the bath is maintained at a value in the range of from about 7 to about 11,
(3) maintaining the bath at a temperature below (4) allowing the material to be plated to remain in the bath until plating in the desired thickness has been achieved, and
(5) removing the plated material from the bath.
3. A process for plating transition metals on nonconductive materials comprising the steps of:
(1) etching the surface of the material to be plated,
( 2) sensitizing the etched surface such that it is catalytic to an electroless transition metal plating bath,
(3) immersing the sensitized material to be plated in an electroless transition metal plating bath comprising an aqueous solution of a nickel-organic compound, a ligand complexing agent for diminishing competition from ions other than reducing and complexing anions for coordination positions of the nickel, a nickel reducing agent, and a carbonate buffering agent wherein the pH of the bath is maintained within the range of from about 7 to 11,
(4) maintaining the bath a a temperature below (5) allowing the material to be plated to remain in the bath until plating in the desired thickness has been achieved, and
(6) removing the plated material from the bath.
4. A process for plating transition metals on nonconductive materials comprising the steps of:
(1) etching the surface of the material to be plated,
(2) depositing a dispersion of a catalytic material on the etched surface,
(3) immersing the material to be plated in an electroless transition metal plating bath comprising an aqueous solution of a nickel-organic coordination compound, a ligand complexing agent selected from the class consisting of glycine, citric acid, carboxypemitic acid, cyanoacetic acid, glycolic acid, propionic acid, formic acid, and salts thereof, a hypophosphite reducing agent, and a carbonate buffering agent wherein the pH of the bath is maintained within the range of from about 7 to about 11,
(4) maintaining the bath at a temperature below (5) allowing the material to be plated to remain in the bath until plating in the desired thickness has been achieved, and
(6) removing the plated material from the bath.
5. A process according to claim 4 wherein the step of depositing a dispersion of a catalytic material on the etched surface comprises the steps of:
(1) immersing the etched material in a first sensitizing bath, and thereafter (2) immersing the material in a second sensitizing bath.
6. A process according to claim 5 wherein the step of etching the surface of the material to be plated comprises placing the material in a chromic acid solution having a specific gravity in the range of 1.6 to 1.68, wherein the step of immersing the etched material in a first sensitizing bath comprises immersing the material in a stannous chloride solution to produce a pre-sensitizing stannous chloride deposit on the etched surface, and wherein the step of immersing the material in a second sensitizing bath comprises immersing the pre-sensitized material in a palladium chloride solution to produce a dispersion of metallic palladium on the etched surface.
7. A process for plating nickel on non-conductive materials comprising the steps of:
(l) etching the surface of the material to be plated,
(2) immersing the etched material in a sensitized bath,
(3) preparing a nickel plating bath by preparing an aqueous solution of nickel glycolate in the range of 1 to 30 grams/liter to which is added glycine in the range of 1 to 50 grams/liter, a nickel reducing agent in the range of 1 to 100 grams/liter, and a carbonate buffering agent in the range of 10 to grams/ liter wherein the pH of the bath is maintained within the range of from about 7 to about 11,
(4) immersing the sensitized material to be plated in the plating bath,
(5) maintaining the plating bath at a temperature below 120 F.,
( 6) allowing the material to be plated to remain in the bath until plating in the desired thickness has been achieved, and
(7) removing the plated material from the bath.
8. A process for plating nickel on non-conductive materials comprising the steps of:
(1) etching the surface of the material to be plated,
(2) immersing the etched material in a first sensitizing bath,
(3) preparing a nickel plating bath by preparing an aqueous solution of nickel acetate in the range of l to 30 grams/ liter to which is added carboxypimelic acid in the range of 1 to 50 grams/liter, a nickel reducing agent in the range of 1 to grams/liter, and a carbonate buffering agent in the range of 10 to 60 grams/liter wherein the pH of the bath is maintained within a range of from about 7 to about 1 1,
(4) immersing the sensitizing material to be plated in the nickel plating bath,
(5) maintaining the nickel plating bath at a temperature below F.,
(6)allowing the material to be plated. to remain in the bath until nickel plating in the desired thickness has been achieved, and
(7) removing the plated material from the bath.
References Cited UNITED STATES PATENTS 2,430,581 11/1947 Pessel 117-130 2,454,610 11/1948 Narcus 11747 R 2,999,770 9/1961 Gutzeit 117-130 3,024,134 3/1962 Nixon et al. 117130 3,140,188 7/1964 Zirngiebl l17-160 X OTHER REFERENCES Narcus: Metallizing of Plastics, Reinhold Pub. Corp. 1960, pp. 16-19, TP1120 N3 Sci. Lib.
RALPH S. KENDALL, Primary Examiner.
US. Cl. X.R. 1061;117--160
US481944A 1965-08-23 1965-08-23 Electroless plating process Expired - Lifetime US3438798A (en)

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Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3484282A (en) * 1966-08-06 1969-12-16 Knapsack Ag Process for the chemical nickel-plating of non-metallic articles
US3533828A (en) * 1968-04-08 1970-10-13 Cosden Oil & Chem Co Metal plating of plastic surfaces
US3537878A (en) * 1969-04-14 1970-11-03 Allied Res Prod Inc Electroless plating process
US3647402A (en) * 1967-10-13 1972-03-07 Dynamit Nobel Ag Galvanically metallized objects having a post-chlorinated polyethylene substrate and process of producing same
US3664860A (en) * 1968-12-06 1972-05-23 Nihon Kagaku Kizai Kk Electrolessly nickel plating on a non-metallic basis material
US3798050A (en) * 1971-05-28 1974-03-19 Ppg Industries Inc Catalytic sensitization of substrates for metallization
US3915716A (en) * 1969-04-17 1975-10-28 Schering Ag Chemical nickel plating bath
US3962495A (en) * 1972-11-08 1976-06-08 Rca Corporation Method of making duplicates of optical or sound recordings
EP0003768A1 (en) * 1978-02-17 1979-09-05 Bayer Ag Metallized paper and process for its manufacture
DE3043462A1 (en) * 1980-11-18 1982-07-08 Licentia Patent-Verwaltungs-Gmbh, 6000 Frankfurt Cobalt-phosphorus thin film - formed by electroless plating from soln. contg. cobalt salt and hypophosphite, and used esp. to mfr. thin film resistors
US5298092A (en) * 1990-05-17 1994-03-29 The Boeing Company Non-chromated oxide coating for aluminum substrates
US5378293A (en) * 1990-05-17 1995-01-03 The Boeing Company Non-chromated oxide coating for aluminum substrates
US5411606A (en) * 1990-05-17 1995-05-02 The Boeing Company Non-chromated oxide coating for aluminum substrates
US5468307A (en) * 1990-05-17 1995-11-21 Schriever; Matthias P. Non-chromated oxide coating for aluminum substrates
US5472524A (en) * 1990-05-17 1995-12-05 The Boeing Company Non-chromated cobalt conversion coating method and coated articles
US5551994A (en) * 1990-05-17 1996-09-03 The Boeing Company Non-chromated oxide coating for aluminum substrates
US5855993A (en) * 1992-04-24 1999-01-05 International Business Machines Corporation Electronic devices having metallurgies containing copper-semiconductor compounds
US5873953A (en) * 1996-12-26 1999-02-23 The Boeing Company Non-chromated oxide coating for aluminum substrates
EP0912641A1 (en) 1997-02-27 1999-05-06 MERCK PATENT GmbH Multilayer interference pigment with transparent central layer
US6432225B1 (en) 1999-11-02 2002-08-13 The Boeing Company Non-chromated oxide coating for aluminum substrates

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US2454610A (en) * 1946-08-13 1948-11-23 Narcus Harold Method for metalization on nonconductors
US2999770A (en) * 1953-08-27 1961-09-12 Gen Am Transport Processes of chemical nickel plating and baths therefor
US3024134A (en) * 1953-07-24 1962-03-06 Gen Motors Corp Nickel chemical reduction plating bath and method of using same
US3140188A (en) * 1960-08-29 1964-07-07 Bayer Ag Bath compositions for chemical plating of metals containing boron nitrogen compounds nd an organic solubilizing compound

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US2430581A (en) * 1944-11-29 1947-11-11 Rca Corp Metallizing nonmetallic bodies
US2454610A (en) * 1946-08-13 1948-11-23 Narcus Harold Method for metalization on nonconductors
US3024134A (en) * 1953-07-24 1962-03-06 Gen Motors Corp Nickel chemical reduction plating bath and method of using same
US2999770A (en) * 1953-08-27 1961-09-12 Gen Am Transport Processes of chemical nickel plating and baths therefor
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Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3484282A (en) * 1966-08-06 1969-12-16 Knapsack Ag Process for the chemical nickel-plating of non-metallic articles
US3647402A (en) * 1967-10-13 1972-03-07 Dynamit Nobel Ag Galvanically metallized objects having a post-chlorinated polyethylene substrate and process of producing same
US3533828A (en) * 1968-04-08 1970-10-13 Cosden Oil & Chem Co Metal plating of plastic surfaces
US3664860A (en) * 1968-12-06 1972-05-23 Nihon Kagaku Kizai Kk Electrolessly nickel plating on a non-metallic basis material
US3537878A (en) * 1969-04-14 1970-11-03 Allied Res Prod Inc Electroless plating process
US3915716A (en) * 1969-04-17 1975-10-28 Schering Ag Chemical nickel plating bath
US3798050A (en) * 1971-05-28 1974-03-19 Ppg Industries Inc Catalytic sensitization of substrates for metallization
US3962495A (en) * 1972-11-08 1976-06-08 Rca Corporation Method of making duplicates of optical or sound recordings
EP0003768A1 (en) * 1978-02-17 1979-09-05 Bayer Ag Metallized paper and process for its manufacture
DE3043462A1 (en) * 1980-11-18 1982-07-08 Licentia Patent-Verwaltungs-Gmbh, 6000 Frankfurt Cobalt-phosphorus thin film - formed by electroless plating from soln. contg. cobalt salt and hypophosphite, and used esp. to mfr. thin film resistors
US5298092A (en) * 1990-05-17 1994-03-29 The Boeing Company Non-chromated oxide coating for aluminum substrates
US5378293A (en) * 1990-05-17 1995-01-03 The Boeing Company Non-chromated oxide coating for aluminum substrates
US5411606A (en) * 1990-05-17 1995-05-02 The Boeing Company Non-chromated oxide coating for aluminum substrates
US5415687A (en) * 1990-05-17 1995-05-16 The Boeing Company Non-chromated oxide coating for aluminum substrates
US5468307A (en) * 1990-05-17 1995-11-21 Schriever; Matthias P. Non-chromated oxide coating for aluminum substrates
US5472524A (en) * 1990-05-17 1995-12-05 The Boeing Company Non-chromated cobalt conversion coating method and coated articles
US5551994A (en) * 1990-05-17 1996-09-03 The Boeing Company Non-chromated oxide coating for aluminum substrates
US5855993A (en) * 1992-04-24 1999-01-05 International Business Machines Corporation Electronic devices having metallurgies containing copper-semiconductor compounds
US5873953A (en) * 1996-12-26 1999-02-23 The Boeing Company Non-chromated oxide coating for aluminum substrates
EP0912641A1 (en) 1997-02-27 1999-05-06 MERCK PATENT GmbH Multilayer interference pigment with transparent central layer
US6432225B1 (en) 1999-11-02 2002-08-13 The Boeing Company Non-chromated oxide coating for aluminum substrates

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