US3513015A - Prevention of skip plating in an electroless nickel bath - Google Patents

Prevention of skip plating in an electroless nickel bath Download PDF

Info

Publication number
US3513015A
US3513015A US635694A US3513015DA US3513015A US 3513015 A US3513015 A US 3513015A US 635694 A US635694 A US 635694A US 3513015D A US3513015D A US 3513015DA US 3513015 A US3513015 A US 3513015A
Authority
US
United States
Prior art keywords
plating
electroless nickel
solution
article
nickel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US635694A
Inventor
James E Fitzpatrick
Wassily Poppe
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Avisun Corp
Original Assignee
Avisun Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Avisun Corp filed Critical Avisun Corp
Application granted granted Critical
Publication of US3513015A publication Critical patent/US3513015A/en
Anticipated expiration legal-status Critical
Assigned to TUBOSCOPE INC., reassignment TUBOSCOPE INC., RELEASED BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: CITICORP NORTH AMERICA, INC.
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31Coating with metals
    • C23C18/32Coating 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
    • C23C18/18Pretreatment of the material to be coated
    • C23C18/20Pretreatment of the material to be coated of organic surfaces, e.g. resins
    • C23C18/28Sensitising or activating

Definitions

  • This invention relates to an improvement in a method for electroplating non-conducting substrates, and more particularly to an improvement in applying a continuous coating to such articles prior to an electroplating step.
  • the plating process may proceed in two ways.
  • the nucleated article is immersed in a treating solution of a copper salt containing a reducing agent such as formaldehyde, trioxymethylene, and the like.
  • a reducing agent such as formaldehyde, trioxymethylene, and the like.
  • Such treatment deposits a thin continuous coating of copper on the surface of the article capable of conducting electricity.
  • the article may then be electroplated with copper by conventional means, followed, if desired by electroplating with nickel and chromium. No difiiculty is usually experienced in depositing a continuous film of electroless copper on the object to be plated.
  • Modern Plastic Encyclopedia Issue, 1967, September 1966, pp. 1019- 1024 For a general description of the plating process see Modern Plastic Encyclopedia Issue, 1967, September 1966, pp. 1019- 1024.
  • the presenece of copper in the plating is undesirable.
  • plated automobile grilles are tested by exposing them to a salt spray. Plated parts in which the base coat is copper corroded badly when subjected to this test. For such applications it is necessary to substitute an electroless nickel coating for the electroless copper coating. Deposition of such electrodes nickel coatings are described in US. Pat. 2,532,283.
  • the foregoing object can be realized by immersing the articles in a weak aqueous solution of hydrogen peroxide for a time of thirty seconds to one minute after the nucleation step but before the electroless nickel step.
  • the articles may be passed directly ot the electroless nickel step from the nucleation step, and only those articles showing skip plating after the electroless nickel step can be contacted with the hydrogen peroxide solution and returned directly to the electroless nickel step.
  • the aqueous hydrogen peroxide solution should contain from about 1% to about 10% by weight of hydrogen peroxide, preferably about 2% to about 5%. Higher concentrations may be used, but the use of stronger solutions only adds to the cost of the process without any improvement in results over the use of the less concentrated solutions.
  • a conditioning solution was made up in the following manner. 18 g. of a composition consisting of 64% by weight of chromium trioxide and 36% of sodium hydrogen sulfate was added to 500 m1. of an inorganic acid composition consisting of 40% by weight of sulfuric acid (96% concentration), 39.5% of phosphoric acid (85% concentration), 3% chromium trioxide, and 17.5% water. The acid solution was heated to C. and 3% by volume of a commercially available mineral spirit having a boil ing point of 159 C.193 C. and consisting predominantly of C C cycloparaffins was added slowly to the acid solution. An exotherm occurred which raised the temperature to C. After about two hours no excess mineral spirit was observed, and the evolution of gas ceased, indicating complete conversion of the mineral spirit into oxidation products. During the reaction about 9% by weight of water was volatilized.
  • plaques were molded from a commercial crystalline polypropylene containing, in addition to the usual stabilizers, 0.5% by weight of Triton X-100, a commercially available detergent of isooctylphenyl polyethoxyethanol. Some of these plaques were immersed in the Conditioning solution described above for ten minutes at 85 C. rinsed in deionized water; dipped in a stannous chloride sensitizing solution containing, per liter of solution, g. of SnCl and 40 ml. of HCl at ambient temperatures for two minutes; again rinsed with water; dipped in a nucleating solution containing, per gallon, 1 g. of palladium chloride an 10 ml. of HCl for two minutes at ambient temperature, and again rinsed with water.
  • plaques are then dipped into an electroless nickel solution containing, per liter, 30 g. of NiCl 50 g. of sodium glycollate, and 10 g. of sodium hypophosphite for minutes at 190 F.
  • the pH of the solution is adjusted to about 5 with caustic soda. After this treatment the plaques are washed and inspected. It is found that extensive skip plating has taken place on some of the plaques.
  • Example 1 The plaques from the control which exhibited skip plating were dipped in a solution made up by mixing one part of a hydrogen peroxide solution with twelve parts of water for one minute at ambient temperatures. They were then returned to the electroless nickel bath and treated for 15 minutes at 190 F. Upon removal from the bath they were found to be uniformly coated with electroless nickel and exhibited no signs of skip plating.
  • Example 2 The procedure of the control was followed using the remainder of the plaques, except that after the nucleation step the plaques were contacted with the hydrogen peroxide solution of claim 1 for one minute prior to immer- U sion in the electroless nickel bath. Upon removal from the electroless nickel bath no skip plating could be observed.
  • the plaques from Examples 1 and 2 were then electroplated with nickel in the conventional manner to deposit a 1 mil film of nickel on the plaque.
  • the bond strength of the plating was 18 lb./in. Bond strength is measured by the pull test in which two parallel cuts are made into the plated metal coating one half inch apart, an additional vertical cut is made to form a tab, one end of the resulting tab is raised suificiently to allow gripping by a tensile testing machine.
  • the specimen is then placed in a tensile tester machine.
  • the specimen is then placed in a tensile tester and the tab is pulled vertically from the surface. The force required to pull the tab is measured as the bond strength.
  • non-conductive article is formed of an acrylonitrile-butadiene-styrene copolymer.

Description

United States Patent 3,513,015 PREVENTION OF SKIP PLATING IN AN ELECTROLESS NICKEL BATH James E. Fitzpatrick, New Castle, Del., and Wassily Poppe, Springfield, Pa. (both Avisun Corporation, P.O. Box 426, Marcus Hook, Pa. 19061) No Drawing. Filed May 3, 1967, Ser. No. 635,694 Int. Cl. C23c 3/02 US. Cl. 117-47 8 Claims ABSTRACT OF THE DISCLOSURE In the art of nickel plating non-conductive articles, skip plating with an electroless nickel plating solution is minimized by contacting the article, after sensitizing with an oxidizable metal salt and nucleating with a noble metal salt, with a hydrogen peroxide solution prior to contact with the electroless nickel plating solution.
This invention relates to an improvement in a method for electroplating non-conducting substrates, and more particularly to an improvement in applying a continuous coating to such articles prior to an electroplating step.
Methods for electroplating articles fabricated from nonconducting materials such as plastics are well known to the art. In such processes it is usual to first clean the article with a mild caustic wash, followed by neutralization; then treating with a conditioning solution consisting of a solution of chromium trioxide in a strong oxidizing mineral acid such as concentrated sulfuric acid or phosphoric acid or mixtures thereof; then sensitizing the surface with a solution of a readily oxid'izable salt such as stannous chloride, which causes the salt to be adsorbed on the surface; followed by a nucleating treatment with an aqueous solution of a noble metal salt such as palladium chloride, which is reduced by the oxidizable salt and forms a metallic film at discrete activated sites.
From this point the plating process may proceed in two ways. In one process the nucleated article is immersed in a treating solution of a copper salt containing a reducing agent such as formaldehyde, trioxymethylene, and the like. Such treatment deposits a thin continuous coating of copper on the surface of the article capable of conducting electricity. The article may then be electroplated with copper by conventional means, followed, if desired by electroplating with nickel and chromium. No difiiculty is usually experienced in depositing a continuous film of electroless copper on the object to be plated. For a general description of the plating process see Modern Plastic Encyclopedia Issue, 1967, September 1966, pp. 1019- 1024.
In certain applications, however, the presenece of copper in the plating is undesirable. For example, plated automobile grilles are tested by exposing them to a salt spray. Plated parts in which the base coat is copper corroded badly when subjected to this test. For such applications it is necessary to substitute an electroless nickel coating for the electroless copper coating. Deposition of such electrodes nickel coatings are described in US. Pat. 2,532,283.
When using electroless nickel, a phenomenon known as skip plating sometimes occurs, in which certain areas of the object to be plated fail to accept the electroless nickel coating, leading to non-adherent electrodeposition of metal on those spots on the surface which were incompletely covered with electroless nickel during subsequent electroplating, or, in extreme cases, the coating is so discontinuous that no plating whatever takes place on such areas. This problem is found in electroplating ABS, but it becomes particularly serious when electroplating polyolefins, such as crystalline polypropylene and high density polyice ethylene. The reason why this phenomenon takes place is not known, but one of many possible theoretical explanations is that Ni++ and H+ ions are competing with each other to plate out or to form a layer on the previously activated sites of the substrate. If the competition is won byNi ions they plate out and form the basis for further nickel plating. If the competition is won by H+ ions they may build up atomic or ionic monolayers, thus interrupting the nickel plating. Whether or not skip plating has or has not taken place can be visually observed when the articles are withdrawn from the electro less nickel bath. If the surface of the article is a uniform shade of dull gray, skip plating has not taken place. If, however, the surface has a mottled appearance, or if shiny areas appear, skip plating has occurred. In the present state of the art, in order to salvage the articles it is necessary to strip the previous coatings from the article, as by dissolution with acid, and to return the article to the first step of the plating process.
It is the object of this invention to prevent skip plating in an electroless nickel bath, and, if such should occur, to provide a method for conditioning the article for return to the electroless nickel bath without the necessity of removing the material previously deposited on the article and recycling it to the first step of the plating article.
We have found that the foregoing object can be realized by immersing the articles in a weak aqueous solution of hydrogen peroxide for a time of thirty seconds to one minute after the nucleation step but before the electroless nickel step. Alternatively, the articles may be passed directly ot the electroless nickel step from the nucleation step, and only those articles showing skip plating after the electroless nickel step can be contacted with the hydrogen peroxide solution and returned directly to the electroless nickel step. The aqueous hydrogen peroxide solution should contain from about 1% to about 10% by weight of hydrogen peroxide, preferably about 2% to about 5%. Higher concentrations may be used, but the use of stronger solutions only adds to the cost of the process without any improvement in results over the use of the less concentrated solutions.
In order that those skilled in the art may more fully appreciate the nature of the invention and of the manner of carrying it out, the following control and examples are given.
CONTROL A conditioning solution was made up in the following manner. 18 g. of a composition consisting of 64% by weight of chromium trioxide and 36% of sodium hydrogen sulfate was added to 500 m1. of an inorganic acid composition consisting of 40% by weight of sulfuric acid (96% concentration), 39.5% of phosphoric acid (85% concentration), 3% chromium trioxide, and 17.5% water. The acid solution was heated to C. and 3% by volume of a commercially available mineral spirit having a boil ing point of 159 C.193 C. and consisting predominantly of C C cycloparaffins was added slowly to the acid solution. An exotherm occurred which raised the temperature to C. After about two hours no excess mineral spirit was observed, and the evolution of gas ceased, indicating complete conversion of the mineral spirit into oxidation products. During the reaction about 9% by weight of water was volatilized.
A number of plaques were molded from a commercial crystalline polypropylene containing, in addition to the usual stabilizers, 0.5% by weight of Triton X-100, a commercially available detergent of isooctylphenyl polyethoxyethanol. Some of these plaques were immersed in the Conditioning solution described above for ten minutes at 85 C. rinsed in deionized water; dipped in a stannous chloride sensitizing solution containing, per liter of solution, g. of SnCl and 40 ml. of HCl at ambient temperatures for two minutes; again rinsed with water; dipped in a nucleating solution containing, per gallon, 1 g. of palladium chloride an 10 ml. of HCl for two minutes at ambient temperature, and again rinsed with water.
The plaques are then dipped into an electroless nickel solution containing, per liter, 30 g. of NiCl 50 g. of sodium glycollate, and 10 g. of sodium hypophosphite for minutes at 190 F. The pH of the solution is adjusted to about 5 with caustic soda. After this treatment the plaques are washed and inspected. It is found that extensive skip plating has taken place on some of the plaques.
Example 1 The plaques from the control which exhibited skip plating were dipped in a solution made up by mixing one part of a hydrogen peroxide solution with twelve parts of water for one minute at ambient temperatures. They were then returned to the electroless nickel bath and treated for 15 minutes at 190 F. Upon removal from the bath they were found to be uniformly coated with electroless nickel and exhibited no signs of skip plating.
Example 2 The procedure of the control was followed using the remainder of the plaques, except that after the nucleation step the plaques were contacted with the hydrogen peroxide solution of claim 1 for one minute prior to immer- U sion in the electroless nickel bath. Upon removal from the electroless nickel bath no skip plating could be observed.
The plaques from Examples 1 and 2 were then electroplated with nickel in the conventional manner to deposit a 1 mil film of nickel on the plaque. The bond strength of the plating was 18 lb./in. Bond strength is measured by the pull test in which two parallel cuts are made into the plated metal coating one half inch apart, an additional vertical cut is made to form a tab, one end of the resulting tab is raised suificiently to allow gripping by a tensile testing machine. The specimen is then placed in a tensile tester machine. The specimen is then placed in a tensile tester and the tab is pulled vertically from the surface. The force required to pull the tab is measured as the bond strength.
What is claimed is:
1. In a process for electroplating non-conductive articles wherein the article is successively contacted with a conditioning solution comprising a strong mineral acid; a sensitizing solution comprising an oxidizable metal salt; a nucleating solution comprising a noble metal salt; and an electroless nickel plating solution comprising a reducible nickel salt; followed by electroplating with nickel, the improvement which consist in contacting the article with an aqueous solution containing at least 1 weight percent of hydrogen peroxide after contact with the nucleating solution and before contacting with the electroless nickel plating solution.
2. The process of claim 1 in which the non-conductive article is formed of polypropylene.
3. The process of claim 1 in which the non-conductive article is formed of polyethylene.
4. The process of claim 1 in which the non-conductive article is formed of an acrylonitrile-butadiene-styrene copolymer.
5. In a process for electroplating non-conductive articles wherein the article is successively contacted with a conditioning solution comprising a strong mineral acid; a sensitizing solution comprising a reducible tin salt; a nucleating solution comprising a noble metal salt; and an electroless nickel plating solution comprising a reducible nickel salt; followed by electroplating with nickel, the improvement which consists in removing from the plating cycle, at the end of the electroless nickel plating step, those articles which show evidence of skip plating, contacting the removed articles with an aqueous hydrogen peroxide solution containing at least 1 weight percent of hydrogen peroxide, and reintroducing the removed articles to the plating cycle at the electroless nickel plating step.
6. The process of claim 5 in which the non-conductive article is polypropylene.
7. The process of claim 5 in which the non-conductive article is polyethylene.
8. The process of claim 5 in which the non-conductive article is an acrylonitrile-butadiene-styrene copolymer.
References Cited UNITED STATES PATENTS 2,690,402 9/ 1954 Crehan. 3,212,918 10/1965 Tsu et a1. 3,265,511 8/1966 Sallo. 3,305,460 2/1967 Lacy. 3,370,974 2/1968 Hepfer.
MURRAY KATZ, Primary Examiner US. Cl. X.R.
831 UNITED STATES PATENT OFFlQi-Q Invontofls) James E. Fitzpatrick and easily Poppe It is car rifled that error av ears in the above-identified atom t and that said Letters Patent are hereby corrected as shorsn below:
I Column 1, line 60, the word "electrodes" should be --electrolesa--. I
Column 2, line 32, the word "at" should be -to--.
Column 3, line 6, the word "an should be --and--. Column Claim 5, line 19, "a reducible" should be --a.n oxidizable--.
smqgg QSEAL) Attcst:
WILLIAM E. sum. Edward M. Fletcher, In c i sioner 01 Patnts Attesting Officer
US635694A 1967-05-03 1967-05-03 Prevention of skip plating in an electroless nickel bath Expired - Lifetime US3513015A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US63569467A 1967-05-03 1967-05-03

Publications (1)

Publication Number Publication Date
US3513015A true US3513015A (en) 1970-05-19

Family

ID=24548741

Family Applications (1)

Application Number Title Priority Date Filing Date
US635694A Expired - Lifetime US3513015A (en) 1967-05-03 1967-05-03 Prevention of skip plating in an electroless nickel bath

Country Status (2)

Country Link
US (1) US3513015A (en)
GB (1) GB1198193A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3647514A (en) * 1968-08-28 1972-03-07 Knapsack Ag Surface-pretreatment of articles made from polyethylene or polypropylene or corresponding copolymers for chemical nickel-plating
US3655433A (en) * 1970-07-06 1972-04-11 Standard Oil Co Platable polymers
US3658569A (en) * 1969-11-13 1972-04-25 Nasa Selective nickel deposition
US4448811A (en) * 1981-12-30 1984-05-15 Omi International Corporation Oxidizing agent for acidic accelerator in electroless metal plating process
WO1985000387A1 (en) * 1983-07-01 1985-01-31 Macdermid, Incorporated Oxidizing accelerator
US4608275A (en) * 1983-07-01 1986-08-26 Macdermid, Incorporated Oxidizing accelerator
US5532024A (en) * 1995-05-01 1996-07-02 International Business Machines Corporation Method for improving the adhesion of polymeric adhesives to nickel surfaces
US6468672B1 (en) 2000-06-29 2002-10-22 Lacks Enterprises, Inc. Decorative chrome electroplate on plastics

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2690402A (en) * 1952-04-01 1954-09-28 Gen Am Transport Processes of chemical nickel plating of nonmetallic bodies
US3212918A (en) * 1962-05-28 1965-10-19 Ibm Electroless plating process
US3265511A (en) * 1963-06-12 1966-08-09 Honeywell Inc Electroless plating
US3305460A (en) * 1964-01-23 1967-02-21 Gen Electric Method of electroplating plastic articles
US3370974A (en) * 1965-10-20 1968-02-27 Ivan C. Hepfer Electroless plating on non-conductive materials

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2690402A (en) * 1952-04-01 1954-09-28 Gen Am Transport Processes of chemical nickel plating of nonmetallic bodies
US3212918A (en) * 1962-05-28 1965-10-19 Ibm Electroless plating process
US3265511A (en) * 1963-06-12 1966-08-09 Honeywell Inc Electroless plating
US3305460A (en) * 1964-01-23 1967-02-21 Gen Electric Method of electroplating plastic articles
US3370974A (en) * 1965-10-20 1968-02-27 Ivan C. Hepfer Electroless plating on non-conductive materials

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3647514A (en) * 1968-08-28 1972-03-07 Knapsack Ag Surface-pretreatment of articles made from polyethylene or polypropylene or corresponding copolymers for chemical nickel-plating
US3658569A (en) * 1969-11-13 1972-04-25 Nasa Selective nickel deposition
US3655433A (en) * 1970-07-06 1972-04-11 Standard Oil Co Platable polymers
US4448811A (en) * 1981-12-30 1984-05-15 Omi International Corporation Oxidizing agent for acidic accelerator in electroless metal plating process
WO1985000387A1 (en) * 1983-07-01 1985-01-31 Macdermid, Incorporated Oxidizing accelerator
US4608275A (en) * 1983-07-01 1986-08-26 Macdermid, Incorporated Oxidizing accelerator
US5532024A (en) * 1995-05-01 1996-07-02 International Business Machines Corporation Method for improving the adhesion of polymeric adhesives to nickel surfaces
US6468672B1 (en) 2000-06-29 2002-10-22 Lacks Enterprises, Inc. Decorative chrome electroplate on plastics

Also Published As

Publication number Publication date
GB1198193A (en) 1970-07-08

Similar Documents

Publication Publication Date Title
US2983634A (en) Chemical nickel plating of magnesium and its alloys
US3682786A (en) Method of treating plastic substrates and process for plating thereon
US4039714A (en) Pretreatment of plastic materials for metal plating
US3437507A (en) Plating of substrates
WO2007122869A1 (en) Composition for etching treatment of resin molded article
US3597266A (en) Electroless nickel plating
US3817774A (en) Preparation of plastic substrates for electroless plating
US4448811A (en) Oxidizing agent for acidic accelerator in electroless metal plating process
US4061802A (en) Plating process and bath
JP6150822B2 (en) Method for metallizing non-conductive plastic surface
JP6180518B2 (en) Method for metallizing non-conductive plastic surfaces
US3524754A (en) Metal plating of plastics
US3513015A (en) Prevention of skip plating in an electroless nickel bath
US3024134A (en) Nickel chemical reduction plating bath and method of using same
US4035227A (en) Method for treating plastic substrates prior to plating
US3867174A (en) Baths for activating the surface of plastics to be chemically metal-plated
US3178311A (en) Electroless plating process
CA2893664C (en) Process for metallizing nonconductive plastic surfaces
US3423226A (en) Plating of non-metallic bodies
US3686017A (en) Surface treatment of nylon shaped articles with aqueous reducing agents
US3619243A (en) No rerack metal plating of electrically nonconductive articles
US3672940A (en) Process for chemically depositing nickel on a synthetic resin base material
US3632388A (en) Preactivation conditioner for electroless metal plating system
US3622370A (en) Method of and solution for accelerating activation of plastic substrates in electroless metal plating system
US5316867A (en) Method for adhering metal coatings to thermoplastic addition polymers

Legal Events

Date Code Title Description
AS Assignment

Owner name: TUBOSCOPE INC.,, TEXAS

Free format text: RELEASED BY SECURED PARTY;ASSIGNOR:CITICORP NORTH AMERICA, INC.;REEL/FRAME:005903/0140

Effective date: 19911028