EP4166690A1 - Electroless gold plating bath - Google Patents

Electroless gold plating bath Download PDF

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Publication number
EP4166690A1
EP4166690A1 EP22197168.2A EP22197168A EP4166690A1 EP 4166690 A1 EP4166690 A1 EP 4166690A1 EP 22197168 A EP22197168 A EP 22197168A EP 4166690 A1 EP4166690 A1 EP 4166690A1
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EP
European Patent Office
Prior art keywords
good good
electroless
plating film
gold
gold plating
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.)
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Application number
EP22197168.2A
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German (de)
English (en)
French (fr)
Inventor
Sayuri Tanaka
Takuma Maekawa
Katsuhisa Tanabe
Fuminori Shibayama
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.)
Uemera Kogyo Co Ltd
C Uyemura and Co Ltd
Original Assignee
Uemera Kogyo Co Ltd
C Uyemura and Co Ltd
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Filing date
Publication date
Application filed by Uemera Kogyo Co Ltd, C Uyemura and Co Ltd filed Critical Uemera Kogyo Co Ltd
Publication of EP4166690A1 publication Critical patent/EP4166690A1/en
Withdrawn legal-status Critical Current

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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
    • C23C18/42Coating with noble metals
    • 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
    • C23C18/42Coating with noble metals
    • C23C18/44Coating with noble metals using reducing agents
    • 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
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F11/00Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
    • C23F11/08Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
    • C23F11/10Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
    • C23F11/14Nitrogen-containing compounds
    • C23F11/149Heterocyclic compounds containing nitrogen as hetero atom
    • 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
    • C23C18/1601Process or apparatus
    • C23C18/1633Process of electroless plating
    • C23C18/1646Characteristics of the product obtained
    • C23C18/165Multilayered product
    • C23C18/1651Two or more layers only obtained by electroless plating
    • 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
    • C23C18/1803Pretreatment of the material to be coated of metallic material surfaces or of a non-specific material surfaces

Definitions

  • the present disclosure relates to an electroless gold plating bath.
  • Gold has high electrical conductivity next to silver and copper, and is excellent in physical properties such as connectivity in thermocompression bonding, and is also excellent in chemical properties such as oxidation resistance and chemical resistance. Therefore, gold plating with gold is widely used as a final surface treatment method for circuits on printed wiring boards, mounting portions and terminal portions of IC packages, and the like in the field of the electronics industry. In recent years, along with the improvement of electronic components to be smaller and denser, electroless plating methods attaining excellent functionality without the need of lead wiring have been used preferably.
  • an Electroless Nickel Immersion Gold (ENIG) process.
  • ENIG Electroless Nickel Immersion Gold
  • ENEPIG Electroless Nickel Electroless Palladium Immersion Gold
  • ENEPIG Electroless Nickel Electroless Palladium Immersion Gold
  • an electroless gold plating bath which contains a water-soluble gold compound, a complexing agent, and a reducing agent as well as polyvinyl alcohol and/or polyvinylpyrrolidone added as a stabilizer. It is described that such a configuration makes it possible to form a good gold plating film only in metal portions and is preferably applicable to gold plating for ceramics IC, packages, and the like (For example, see Japanese Patent No.2927142 ).
  • an object of the present disclosure is to provide an electroless gold plating bath, which is capable of forming a uniform gold plating film with a sufficient thickness in one step in both the ENIG process and the ENEPIG process.
  • the electroless gold plating bath of the present disclosure includes a gold sulfite, a thiosulfate, ascorbic acid compounds, and hydrazine compounds, the hydrazine compounds being at least one selected from the group consisting of adipic dihydrazide, propionic hydrazide, hydrazine sulfate, hydrazine monohydrochloride, hydrazine dihydrochloride, hydrazine carbonate, hydrazine monohydrate, sebacic dihydrazide, dodecanediohydrazide, isophthalic dihydrazide, salicylic hydrazide, 3-hydro-2-naphthoic hydrazide, benzophenone hydrazone, phenylhydrazine, benzylhydrazine monohydrochloride, methylhydrazine sulfate, isopropylhydrazine hydrochloride, 1,
  • an electroless gold plating bath which is capable of forming a uniform gold plating film with a sufficient thickness in one step in both the ENIG process and the ENEPIG process.
  • the electroless gold plating bath of the present disclosure is an electroless gold plating bath including a gold sulfite as a gold source, a thiosulfate as a complexing agent, ascorbic acid compounds as a reducing agent, and hydrazine compounds as a reducing agent.
  • the electroless gold plating bath of the present disclosure is a cyanide-free bath (non-cyanide bath), and includes, as the gold source, gold sulfite (e.g., sodium gold sulfite), which is a water-soluble gold compound with no cyano group.
  • gold sulfite e.g., sodium gold sulfite
  • the concentration of the gold sulfite in the plating bath may be preferably 0.5 g/L to 2 g/L based on gold.
  • a concentration of the gold sulfite of less than 0.5 g/L would result in a low plating deposition rate, while a concentration of the gold sulfite of more than 2 g/L would result in a poor adhesion of the gold plating film to the electroless nickel plating film.
  • the complexing agent is used to stabilize the solubility of gold in the electroless gold plating bath.
  • the electroless gold plating bath of the present disclosure includes a sulfur compound as the complexing agent.
  • the sulfur compound may be a thiosulfate (such as sodium thiosulfate, potassium thiosulfate, ammonium thiosulfate, or the like) a sulfite (such as sodium sulfite, potassium sulfite, ammonium sulfite, or the like).
  • thiosulfate such as sodium thiosulfate, potassium thiosulfate, ammonium thiosulfate, or the like
  • a sulfite such as sodium sulfite, potassium sulfite, ammonium sulfite, or the like.
  • the concentration of the thiosulfate (which may be thiosulfates) in the plating bath may be in a range of 0.5 g/L to 10 g/L, preferably. If the concentration of the thiosulfate is less than 0.5 g/L. the effect of the complexing agent would be insufficient, and if the concentration of the thiosulfate is greater than 10 g/L, local corrosion of the electroless nickel plating film would be increased, which would cause a gap between the corroded portion of the electroless nickel plating film and the electroless gold plating film, thereby reducing adhesion of the gold plating film to the electroless nickel plating film.
  • the reducing agent is used to reduce the gold sulfite, which is the gold source, in order to precipitate gold.
  • the reducing agent includes hydrazine compounds and ascorbic acid compounds in combination used at once.
  • the hydrazine compounds are for facilitating the formation of the gold plating film on the nickel plating film or the palladium plating film, especially for facilitating the formation of the gold plating film on the palladium plating film in the ENEPIG process.
  • hydrazine compounds examples include adipic dihydrazide, propionic hydrazide, hydrazine sulfate, hydrazine monohydrochloride, hydrazine dihydrochloride, hydrazine carbonate, hydrazine monohydrate, sebacic dihydrazide, dodecanediohydrazide, isophthalic dihydrazide, salicylic hydrazide, 3-hydro-2-naphthoic hydrazide, benzophenone hydrazone, phenylhydrazine, benzylhydrazine monohydrochloride, methylhydrazine sulfate, isopropylhydrazine hydrochloride, 1,1-dimethyhydrazine, 2-hydrazinobenzothiazole, acetohydrazide, 2-hydroxyethylhydrazine, ethoxycarbonylhydrazine, methoxycarbonylhydr
  • the concentration of the hydrazine compound (which may be hydrazine compounds) in the plating bath may be in a range of 0.5 g/L to 15 g/L., preferably. If the concentration of the hydrazine is less than 0.5 g/L, a plating rate would become insufficient. Moreover, in general, the plating rate is increased proportionally to the concentration of the reducing agent. However, if the concentration of the hydrazine is greater than 15 g/L, the plating rate would not be improved so significantly regardless of the concentration, while bath stability of the plating bath would be deteriorated.
  • the ascorbic acid compounds are for improving the deposition property of the gold plating on the gold plating film deposited by the hydrazine compounds so as to facilitate the formation of the gold plating film, and the ascorbic acid compounds make it possible to form a gold plating film with a sufficient thickness (of 0.1 ⁇ m or thicker).
  • ascorbic acid compounds examples include alkali metal salts such as ascorbic acid and sodium ascorbyl phosphate, alkali earth metal salts such as magnesium ascorbyl phosphate, esters such as ascorbic acid 2-glucoside, and the like. These ascorbic acid compounds may be used solely, or a combination of two or more thereof may be used.
  • the concentration of the ascorbic acid compound (which may be ascorbic acid compounds) in the plating bath may be in a range of 1 g/L to 20 g/L, preferably. If the concentration of the ascorbic acid is less than 1 g/L, the plating rate would become insufficient, and if the concentration of the ascorbic acid is greater than 20 g/L, the plating rate would not be improved so significantly regardless of the concentration, while bath stability of the plating bath would be deteriorated.
  • the electroless gold plating bath of the present disclosure is configured as follows:
  • the reducing agent includes a combination of the hydrazine compounds and the ascorbic acid compounds used at once, the hydrazine compounds being capable of facilitating the formation of the gold plating film on the nickel plating film and the palladium plating film, and the hydrazine compounds being capable of facilitating the formation of the gold plating film by improving the deposition property of the gold plating on the gold plating film deposited by the hydrazine compounds, thereby making it possible to form a uniform gold plating film (that is, uniform in outer appearance and excellent in the deposition property) with a sufficient thickness (of 0.1 ⁇ m or thicker) in one step process either in the ENIG process or ENEPIG process.
  • An amine-based complexing agent is for improving the adhesion of the gold plating film to the electroless nickel plating film, and the electroless gold plating bath of the present disclosure includes an ethyleneamine as the amine-based complexing agent.
  • ethyleneamine examples include ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine, and the like. These polyethyleneamines may be used solely, or a combination of two or more thereof may be used.
  • the concentration of the amine-based complexing agent in the plating bath may be in a range of 0.5 g/L to 10 g/L, preferably.
  • the plating bath of the present disclosure may be configured such that the electroless gold plating bath further includes a known additive(s) of various kinds, if necessary.
  • the additive include an anti-corrosion agent, an electric conducting salt, and the like.
  • the anti-corrosion agent is an agent for preventing the corrosion on the surfaces of the nickel plating film and palladium plating film.
  • the anti-corrosion agent is not particularly limited, but for example, the anti-corrosion agent may be 1,2,3-benzotriazole, 1,2,4-triazole, 3-amino-1,2,4-triazole, 3-mercapto-1,2,4-triazole, 3-carboxamido-1,2,4-triazole, 3-aminopyrrolidine, 3-aminopyrazole, or the like.
  • the concentration of the anti-corrosion agent in the plating bath may be in a range of 0.1 g/L to 2 g/L, preferably.
  • examples of the electric conducting salt include sodium succinate, trisodium citrate, sodium malate, disodium malonate, sodium oxalate, disodium glutarate, sodium tartrate, and the like.
  • the concentration of the electric conducting salt in the plating bath may be in a range of 5 g/L to 100 g/L, preferably.
  • the formation of the gold plating film with the sufficient thickness (of 0.1 ⁇ m or thicker) on the surface of the nickel plating film and/or the palladium plating film would result in deterioration of the adhesion of the gold plating film to the electroless nickel plating film and/or corrosion on the surface of the electroless nickel plating film and/or the electroless palladium plating film.
  • pH of the electroless gold plating bath of the present disclosure is in a range of 6 to 9. If the pH is less than 6, the plating rate would be insufficient, and if pH is greater than 9, the plating bath would be unstable.
  • the pH of the plating bath can be adjusted by a pH adjuster such as sodium hydroxide, potassium hydroxide, ammonia water, tetramethyl ammonium hydroxide, sulfuric acid, hydrochloric acid, boric acid, phosphoric acid, monocarboxylic acid, or dicarboxylic acid.
  • a pH adjuster such as sodium hydroxide, potassium hydroxide, ammonia water, tetramethyl ammonium hydroxide, sulfuric acid, hydrochloric acid, boric acid, phosphoric acid, monocarboxylic acid, or dicarboxylic acid.
  • the temperature of the plating bath is not particularly limited, but may be in a range of 50°C to 80°C, preferably. If the temperature of the plating bath is less than 50°C, a deposition rate would be excessively slow, which would result in a long plating time, undesirably. If the temperature of the plating bath is higher than 80°C, the deposition rate would be excessively fast, which would produce coarse films, which would cause warping of a substrate due to thermal shrinkage of the films after the plating. Thus, such a high temperature of the plating bath is not preferable.
  • the electroless gold plating bath of the present disclosure is applicable to any kinds of plating objects, and is applicable to plating objects which have been treated with known electroless gold plating processes (for example, wiring circuits, terminal portions, and the like of electronic parts such as printed wiring boards, ceramics substrates, semiconductor substrates, IC packages, and the like).
  • the electroless gold plating bath according to the present disclosure is, for example, electroless gold plating process in the ENIG process and the ENEPIG process.
  • an electroless gold plating film can be formed on a palladium plating film by implementing the electroless gold plating bath according to the present disclosure in such a way that a surface of a palladium plating film is subjected to the electroless gold plating process by immersing the palladium plating film in the electroless gold plating film.
  • the temperature of the electroless gold plating process is adjusted to the bath temperature of the electroless gold plating bath described above.
  • a process time of the electroless gold plating process is not particularly limited and may be adjusted as appropriate to attain a desired film thickness. More specifically, the electroless gold plating process may be, for example in a range of 30 sec to 15 hours, approximately.
  • An electroless gold plating bath of Example 1 was prepared by mixing and stirring a gold sulfite (sodium gold sulfite), sodium succinate as the electric conducting salt, sodium thiosulfate and disodium sulfite as the complexing agent, 1,2,3-benzotriazole as the anti-corrosion agent, ethylenediamine as the amine-based complexing agent, and ascorbic acid and adipic dihydrazide as the reducing agent with concentrations listed in Table 1.
  • the plating bath was set to a temperature (i.e., temperature of the plating processing) of 70°C, and the pH was set to 7.5.
  • Step 1 A substrate (TEG wafer) was treated with a degreasing cleaning treatment (50°C, 300 sec) with a degreasing cleaner (EPITHAS MCL-16 (product name) available from C. Uyemura & Co., Ltd.).
  • a degreasing cleaning treatment 50°C, 300 sec
  • a degreasing cleaner EPITHAS MCL-16 (product name) available from C. Uyemura & Co., Ltd.
  • Step 2 Next, the substrate was treated with a pickling treatment (21°C, 30 sec) with a nitric acid solution of 30 wt%, thereby forming an oxide film on the surface of the substrate.
  • Step 3 Next, the substrate was treated with a primary zincate treatment (21°C, 20 sec) with a zincate treatment bath (with EPITHAS MCT-51 (product name) available from C. Uyemura & Co., Ltd.).
  • a primary zincate treatment 21°C, 20 sec
  • a zincate treatment bath with EPITHAS MCT-51 (product name) available from C. Uyemura & Co., Ltd.
  • Step 4 The substrate was treated with a pickling treatment (21°C, 60 sec) with the nitric acid solution of 30 wt%, so as to peel off the zincate film and forming an oxide film on the surface of the substrate.
  • Step 5 Next, the substrate was treated with a secondary zincate treatment (21°C, 40 sec) with a zincate treatment bath (with EPITHAS MCT-51 (product name) available from C. Uyemura & Co., Ltd.).
  • a secondary zincate treatment 21°C, 40 sec
  • a zincate treatment bath with EPITHAS MCT-51 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate thus prepared was treated with an electroless plating process (80°C, 15 min) with a nickel-phosphorus plating bath (with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a nickel plating film (a nickel plating film with a phosphorus concentration of 6% to 8% in the film and a thickness of 3 ⁇ m) on the substrate.
  • a nickel-phosphorus plating bath with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the nickel plating film thereon was immersed for 15 min in the plating bath prepared as above, thereby forming an electroless gold plating film on the plating object.
  • the substrate thus treated with the electroless gold plating process was visually observed in terms of tonal change of the outer appearance of the substrate due to the gold deposition, so as to evaluate the deposition property of the gold plating film formed by the plating process.
  • the evaluation found that the surface color of the substrate had been changed to yellow, confirming gold deposition.
  • the substrate thus prepared was treated with an electroless plating process (80°C, 15 min) with a nickel-phosphorus plating bath (with EPITHAS NLL-1 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a nickel plating film (a nickel plating film with a phosphorus concentration of 2% to 4% in the film and a thickness of 3 ⁇ m) on the substrate.
  • a nickel-phosphorus plating bath with EPITHAS NLL-1 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the nickel plating film thereon was immersed for 15 min in the plating bath prepared as above, thereby forming an electroless gold plating film on the plating object.
  • the substrate was evaluated in terms of the deposition property of the plating, finding a surface color change of the substrate to yellow and thereby confirming gold deposition.
  • the substrate thus prepared was treated with an electroless plating process (80°C, 15 min) with a nickel-bismuth plating bath (with EPITHAS KSB-18 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a nickel plating film (with a thickness of 3 ⁇ m) on the substrate.
  • a nickel-bismuth plating bath with EPITHAS KSB-18 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the nickel plating film thereon was immersed for 15 min in the plating bath prepared as above, thereby forming an electroless gold plating film on the plating object.
  • the substrate was evaluated in terms of the deposition property of the plating, finding a surface color change of the substrate to yellow and thereby confirming gold deposition.
  • the substrate thus prepared was treated with an electroless plating process (80°C, 15 min) with a nickel-phosphorus plating bath (with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a nickel plating film (with a thickness of 3 ⁇ m) on the substrate.
  • a nickel-phosphorus plating bath with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate was treated with an electroless plating process (56°C, 15 min) with a palladium plating bath (with EPITHAS TFP-25 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a palladium plating film (with a thickness of 0.3 ⁇ m) on the nickel plating film.
  • a palladium plating bath with EPITHAS TFP-25 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the palladium plating film was immersed for 15 min in the plating bath prepared as above, thereby forming an electroless gold plating film on the plating object.
  • the plating object was evaluated in terms of the deposition property of the plating, finding a surface color change of the substrate to yellow and thereby confirming gold deposition.
  • the substrate thus prepared was treated with an electroless plating process (80°C, 15 min) with a nickel-phosphorus plating bath (with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a nickel plating film (with a thickness of 3 ⁇ m) on the substrate.
  • a nickel-phosphorus plating bath with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate thus prepared was treated with an electroless plating process (50°C, 15 min) with a palladium-phosphorus plating bath (with EPITHAS TFP-30 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a palladium plating film (with a thickness of 0.15 ⁇ m) on the nickel plating film.
  • a palladium-phosphorus plating bath with EPITHAS TFP-30 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the palladium plating film was immersed for 15 min in the plating bath prepared as above, thereby forming an electroless gold plating film on the plating object.
  • the substrate was evaluated in terms of the deposition property of the plating, finding a surface color change of the substrate to yellow and thereby confirming gold deposition.
  • the substrate thus prepared was treated with an electroless plating process (80°C, 15 min) with a nickel-phosphorus plating bath (with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a nickel plating film (with a thickness of 3 ⁇ m) on the substrate.
  • a nickel-phosphorus plating bath with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate thus prepared was treated with an electroless plating process (78°C, 7 min) with a platinum plating bath (with EPITHAS TAE-30 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a platinum plating film (with a thickness of 0.2 ⁇ m) on the nickel plating film.
  • a platinum plating bath with EPITHAS TAE-30 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the platinum plating film thereon was immersed for 15 min in the plating bath prepared as above, thereby forming an electroless gold plating film on the plating object.
  • the substrate was evaluated in terms of the deposition property of the plating, finding a surface color change of the substrate to yellow and thereby confirming gold deposition.
  • the substrate thus prepared was treated with an electroless plating process (75°C, 60 min) with a cobalt-tungsten-phosphorus plating bath (with EPITHAS HWP-5 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a cobalt alloy plating film (with a thickness of 0.3 ⁇ m) on the substrate.
  • a cobalt-tungsten-phosphorus plating bath with EPITHAS HWP-5 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the cobalt alloy plating film thereon was immersed for 15 min in the plating bath prepared as above, thereby forming an electroless gold plating film on the plating object.
  • the substrate was evaluated in terms of the deposition property of the plating, finding a surface color change of the substrate to yellow and thereby confirming gold deposition.
  • the substrate thus prepared was treated with an electroless plating process (75°C, 60 min) with a cobalt-tungsten-boron plating bath (with EPITHAS HWB-31 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a cobalt alloy plating film (with a thickness of 0.5 ⁇ m) on the substrate.
  • a cobalt-tungsten-boron plating bath with EPITHAS HWB-31 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the cobalt alloy plating film thereon was immersed for 15 min in the plating bath prepared as above, thereby forming an electroless gold plating film on the plating object.
  • the substrate was evaluated in terms of the deposition property of the plating, finding a surface color change of the substrate to yellow and thereby confirming gold deposition.
  • the electroless gold plating bath according to the present disclosure As described above, it was confirmed that gold was successfully deposited by the use of the electroless gold plating bath according to the present disclosure in any of the cases where the base plating film was the electroless nickel-phosphorus plating film, the electroless nickel-bismuth plating film, the electroless palladium plating film, the electroless palladium-phosphorus plating film, the electroless platinum plating film, or the electroless cobalt alloy plating film, thereby confirming that the electroless gold plating bath according to the present disclosure could work usefully.
  • Electroless gold plating baths of Examples 1 to 48 and Comparative Examples 1 to 9 were prepared by mixing and stirring a gold sulfite (sodium gold sulfite), sodium succinate as the electric conducting salt, sodium thiosulfate and disodium sulfite as the complexing agent, 1,2,3-benzotriazole as the anti-corrosion agent, an amine-based complexing agent, and ascorbic acid compounds and hydrazine compounds as the reducing agent with concentrations listed in Tables 2 to 6.
  • the plating bath was set to a temperature (i.e., temperature of the plating processing) in a range of 50°C to 80°C, and the pH was set in a range of 6 to 9.
  • the substrate thus prepared was treated with an electroless plating process (80°C, 15 min) with a nickel-phosphorus plating bath (with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a nickel plating film (with a thickness of 3 ⁇ m) on the substrate.
  • a nickel-phosphorus plating bath with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the nickel plating film thereon was immersed for 15 min in the plating bath of one of Examples 1 to 48 and Comparative Examples 1 to 9, thereby forming an electroless gold plating film on the nickel plating film.
  • the substrate thus prepared was treated with an electroless plating process (80°C, 15 min) with a nickel-phosphorus plating bath (with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a nickel plating film (with a thickness of 3 ⁇ m) on the substrate.
  • a nickel-phosphorus plating bath with EPITHAS NPR-18 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate was treated with an electroless plating process (56°C, 15 min) with a palladium plating bath (with EPITHAS TFP-25 (product name) available from C. Uyemura & Co., Ltd.), thereby forming a palladium plating film (with a thickness of 0.3 ⁇ m) on the nickel plating film.
  • a palladium plating bath with EPITHAS TFP-25 (product name) available from C. Uyemura & Co., Ltd.
  • the substrate with the nickel plating film thereon was immersed for 15 min in the plating bath of one of Examples 1 to 48 and Comparative Examples 1 to 9, thereby forming an electroless gold plating film on the palladium plating film.
  • a sample of the electroless gold plating film with a size of 2.5 cm ⁇ 2.5 cm was prepared.
  • An adhesive cellophane tape with a width of approximately 2 cm was adhered to a surface of the electroless gold plating film and manually peeled off from the surface. If the electroless gold plating film was not peeled off together with the tape, the electroless gold plating film was evaluated as good, and if peeled off, the electroless gold plating film was evaluated as poor.
  • the results of the evaluation are presented in Tables 2 to 6.
  • the surfaces of the electroless gold plating film were observed with a scanning electron microscope (SEM, available from JEOL Ltd.) to evaluate in such a way that films with uniform gold plating deposition were evaluated as good, and films with non-uniform gold plating deposition, in which gold deposition was partially unsuccessful, were evaluated as poor.
  • SEM scanning electron microscope
  • the electroless gold plating film was peeled off, and a base film of the electroless gold plating film (the surface of the electroless nickel plating film in the case of the ENIG process and the electroless nickel plating film under the electroless palladium plating film in the case of ENEPIG process) was observed by a scanning electron microscope, and a cross-section thereof was observed with a focused ion beam (FIB) device (available from Hitachi High-Tech Corporation), evaluating as poor if the electroless nickel plating film has corrosion on the surface or the cross-section thereof (that is, if the electroless nickel plating film has a hole on the surface or a hole or staining on the cross-section) and evaluating as good if the electroless nickel plating film had no such corrosion.
  • the results of the evaluation are presented in Tables 2 to 6.
  • the electroless gold plating baths of Examples 1 to 48 including a gold sulfite, a thiosulfate, ascorbic acid compounds, and hydrazine compounds, wherein a combination of the hydrazine compounds and the ascorbic acid serve as a reducing agent, make it possible to form a uniform gold plating film (that is, uniform in outer appearance and excellent in the deposition property) with a sufficient thickness (of 0.1 ⁇ m or thicker) by a single-step process either in the ENIG process or ENEPIG process, because the hydrazine compounds capable of facilitating the formation of the gold plating film on the nickel plating film or the palladium plating film and the ascorbic acid compounds capable of facilitating the formation of the gold plating film by improving the deposition property of the gold plating on the gold plating film deposited by the hydrazine are used at once.
  • Comparative Example 1 without hydrazine compounds was poor in the outer appearance and deposition property, and the gold plating film thereof was not uniform, as understood from Table 6.
  • Comparative Example 2 without ascorbic acid compounds was poor in the deposition property, and the gold plating film thereof was not uniform.
  • Comparative Example 3 without a sodium thiosulfate was unstable in gold solubility in the electroless gold plating bath and poor in the outer appearance and deposition property, and the gold plating film thereof was not uniform.
  • Comparative Example 6 without ethylene diamine was poor in the adhesion of the gold plating film to the electroless nickel plating film.
  • Comparative Example 8 without an anti-corrosion agent was poor in the adhesion of the gold plating film to the electroless nickel plating film, because local corrosions increased on the electroless nickel plating film, causing gaps between the corroded portion of the electroless nickel plating film and the electroless gold plating film.
  • the electroless gold plating bath according to the present disclosure is suitably applicable especially to formation of an electroless gold plating film in the ENIG process and the ENEPIG process.

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  • Engineering & Computer Science (AREA)
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  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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EP22197168.2A 2021-10-13 2022-09-22 Electroless gold plating bath Withdrawn EP4166690A1 (en)

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JP2021168259A JP2023058312A (ja) 2021-10-13 2021-10-13 無電解金めっき浴

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US (1) US20230111446A1 (zh)
EP (1) EP4166690A1 (zh)
JP (1) JP2023058312A (zh)
KR (1) KR20230052819A (zh)
CN (1) CN115961273A (zh)
TW (1) TW202331000A (zh)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5364460A (en) * 1993-03-26 1994-11-15 C. Uyemura & Co., Ltd. Electroless gold plating bath
EP0618308B1 (en) * 1993-03-26 1998-06-17 C. Uyemura & Co, Ltd Electroless gold plating bath
JP2013224496A (ja) * 2013-08-07 2013-10-31 Japan Pure Chemical Co Ltd 金めっき液用亜硫酸金塩水溶液
JP2017025399A (ja) * 2015-07-28 2017-02-02 上村工業株式会社 ノンシアン無電解金めっき浴および無電解金めっき方法

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5364460A (en) * 1993-03-26 1994-11-15 C. Uyemura & Co., Ltd. Electroless gold plating bath
EP0618308B1 (en) * 1993-03-26 1998-06-17 C. Uyemura & Co, Ltd Electroless gold plating bath
JP2927142B2 (ja) 1993-03-26 1999-07-28 上村工業株式会社 無電解金めっき浴及び無電解金めっき方法
JP2013224496A (ja) * 2013-08-07 2013-10-31 Japan Pure Chemical Co Ltd 金めっき液用亜硫酸金塩水溶液
JP2017025399A (ja) * 2015-07-28 2017-02-02 上村工業株式会社 ノンシアン無電解金めっき浴および無電解金めっき方法

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CN115961273A (zh) 2023-04-14
KR20230052819A (ko) 2023-04-20

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