WO2008059789A1 - Silver-plated fine copper powder, conductive paste produced from silver-plated fine copper powder, and process for producing silver-plated fine copper powder - Google Patents
Silver-plated fine copper powder, conductive paste produced from silver-plated fine copper powder, and process for producing silver-plated fine copper powder Download PDFInfo
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- WO2008059789A1 WO2008059789A1 PCT/JP2007/071907 JP2007071907W WO2008059789A1 WO 2008059789 A1 WO2008059789 A1 WO 2008059789A1 JP 2007071907 W JP2007071907 W JP 2007071907W WO 2008059789 A1 WO2008059789 A1 WO 2008059789A1
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- silver
- fine powder
- copper fine
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- fine copper
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/02—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of metals or alloys
- H01B1/023—Alloys based on aluminium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
- B22F1/17—Metallic particles coated with metal
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/1601—Process or apparatus
- C23C18/1633—Process of electroless plating
- C23C18/1635—Composition of the substrate
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/1601—Process or apparatus
- C23C18/1633—Process of electroless plating
- C23C18/1655—Process features
- C23C18/166—Process features with two steps starting with addition of reducing agent followed by metal deposition
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/1601—Process or apparatus
- C23C18/1633—Process of electroless plating
- C23C18/1689—After-treatment
- C23C18/1692—Heat-treatment
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/18—Pretreatment of the material to be coated
- C23C18/1803—Pretreatment of the material to be coated of metallic material surfaces or of a non-specific material surfaces
- C23C18/1824—Pretreatment of the material to be coated of metallic material surfaces or of a non-specific material surfaces by chemical pretreatment
- C23C18/1837—Multistep pretreatment
- C23C18/1844—Multistep pretreatment with use of organic or inorganic compounds other than metals, first
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/31—Coating with metals
- C23C18/42—Coating with noble metals
- C23C18/44—Coating with noble metals using reducing agents
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/54—Contact plating, i.e. electroless electrochemical plating
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/02—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of metals or alloys
- H01B1/026—Alloys based on copper
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/20—Conductive material dispersed in non-conductive organic material
- H01B1/22—Conductive material dispersed in non-conductive organic material the conductive material comprising metals or alloys
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F2999/00—Aspects linked to processes or compositions used in powder metallurgy
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- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K1/00—Printed circuits
- H05K1/02—Details
- H05K1/09—Use of materials for the conductive, e.g. metallic pattern
- H05K1/092—Dispersed materials, e.g. conductive pastes or inks
- H05K1/095—Dispersed materials, e.g. conductive pastes or inks for polymer thick films, i.e. having a permanent organic polymeric binder
Definitions
- Silver-plated copper fine powder conductive paste produced using silver-plated copper fine powder, and method for producing silver-plated copper fine powder
- the present invention relates to a silver-plated copper fine powder, a conductive paste produced using the silver-plated copper fine powder, and a method for producing the silver-plated copper fine powder, and is particularly excellent in conductivity and reproducibility during the silver-plated reaction.
- the present invention relates to a silver-plated copper fine powder having a tap density comparable to that of the raw material copper fine powder.
- Conductive pastes are widely used from experimental purposes to applications in the electronics industry because of their ease of contact.
- silver-plated copper fine powder with a silver layer coated on its surface is processed into a conductive paste and applied to circuit formation of printed wiring boards using a screen printing method, various electrical contact portions, etc. It has been used as a material for ensuring electrical continuity.
- the silver-plated copper fine powder is more excellent in electrical conductivity than the copper fine powder when compared with normal copper fine powder that does not cover the surface with a silver layer.
- silver powder alone is expensive, but if silver is attached to copper, the conductive powder as a whole will be inexpensive and the production cost can be greatly reduced. Therefore, a conductive paste made of fine copper powder coated with silver, which is superior in conductive properties, has a great advantage if a low-resistance conductor can be manufactured at low cost.
- Patent Document 1 describes a method of substituting and depositing silver on the surface of metallic copper powder using a silver complex solution of silver nitrate, ammonium carbonate, and ethylenediamine tetraacetate.
- Patent Document 2 discloses a method in which copper powder is dispersed in a chelating agent solution, a silver nitrate solution is added to the copper powder dispersion, a reducing agent is added in the next step, and a silver film is deposited on the surface of the copper powder. Is disclosed. Furthermore, in Patent Document 3, a chelating agent is added to a copper powder dispersion to prepare a copper powder slurry, and a buffer is added thereto to adjust pH, and then silver ions are added to this for a substitution reaction. A technique for making silver-coated copper powder is disclosed.
- the silver-plated copper fine powder obtained by these production methods is excellent in electrical conductivity and moisture resistance, and has been used as a suitable material as a conductive paste material.
- the silver-plated copper fine powders obtained by these manufacturing methods have variations in the color tone after the silver-plated reaction due to the oxidation state of the copper fine powder before the silver-plated, and the tap density is reduced by the silver-plated, etc. I had a problem.
- Patent Document 1 JP-A-57-59283
- Patent Document 2 JP-A-2-46641
- Patent Document 2 JP 2004-52044 A
- the present invention aims to solve the above-described problems, and is a silver-plated copper fine powder having excellent conductivity and reproducibility during a silver-plated reaction, and having a tap density similar to that of the raw copper fine powder, and a method for producing the same. Provide law.
- the present inventors have introduced a surface treatment step before and after the silver plating reaction in the conventional silver plating copper fine powder, and electroless substitution plating and reduction type.
- a silver layer on the surface of the copper fine powder by plating it was found that the silver-plated copper fine powder was excellent in reproducibility during the production of silver plating and had a tap density similar to that of the raw copper powder.
- Silver-plated copper fine powder with average particle size ! ⁇ 30 111, tap density 2.4 g / cm 3 or more, specific surface area 0.9 m 2 / g or less
- Silver-plated copper fine powder with an average particle size of 3 to 20 111, tap density of 3. Og / cm 3 or more, and specific surface area of 0.6 mg or less
- the present invention also provides
- the silver-plated copper fine powder manufacturing method that forms a silver layer on the surface of the copper fine powder, remove the copper fine powder from the organic matter on the surface of the copper fine powder in an alkaline solution. After pickling and washing the product, a reducing agent is added to the acidic solution in which the copper fine powder is dispersed to adjust the pH to create a copper fine powder slurry, and a silver ion solution is continuously added to the copper fine powder slurry.
- the silver plating copper fine powder is immersed in an alcohol solution containing a fatty acid, and the surface of the silver plating copper fine powder is coated with 0.01 to 5.0 wt% of fatty acid.
- the silver plating copper fine powder is immersed in an alcohol solution containing a fatty acid, and the surface of the silver plating copper fine powder is coated with 0.;! To 1.0% by weight of fatty acid.
- a method for producing a silver-plated copper fine powder is
- the surface of the copper fine powder is uniformly coated by introducing a surface treatment step before and after the silver plating reaction and forming a silver layer on the surface of the copper fine powder by electroless substitution plating and reduction type plating.
- a surface treatment step before and after the silver plating reaction
- a silver layer on the surface of the copper fine powder by electroless substitution plating and reduction type plating.
- it has excellent conductivity and reproducibility at the time of silver plating reaction, resulting in silver plating copper fine powder with tap density comparable to that of raw copper fine powder, which is stable when used in conductive paste.
- it has an excellent effect that high filling can be achieved.
- the copper hydroxide may be re-precipitated when taken out as a powder.
- the silver ion solution was charged all together during the substitution reaction, it was considered that the silver ion concentration became non-uniform around the copper powder, and silver-plated copper fine powder with poor silver coating was formed.
- the present invention removes the organic matter on the surface of the copper fine powder by dispersing the copper fine powder in the alkaline solution, and removes the oxide on the surface of the copper fine powder by dispersing the copper fine powder in the acidic solution.
- the pH is adjusted so that the copper ions complexed by the agent can be maintained in a stable state, and the silver ion solution is continuously added so that the substitution reaction with silver ions proceeds uniformly.
- the silver layer can be coated extremely uniformly on the surface of the copper fine powder.
- Sodium hydroxide, potassium hydroxide, or the like is used as the alkaline solution.
- An alkaline solution that can reliably remove the organic matter on the surface of the copper fine powder before the substitution reaction is preferred, but potassium hydroxide is preferred.
- an acidic solution sulfuric acid, hydrochloric acid, phosphoric acid or the like is used. It is preferable to use sulfuric acid, and it should be an acidic solution that can reliably remove the copper oxide on the surface of the copper fine powder before the substitution reaction. The selected type and concentration should not excessively dissolve the copper fine copper itself. there is a need force s to.
- the pH of this acidic solution is preferably in the acidic range of 2 ⁇ 0 to 5 ⁇ 0. When ⁇ exceeds 5.0, oxides of copper fine powder cannot be sufficiently dissolved and removed, and when pH is lower than 2.0, copper powder dissolves and the copper fine powder itself tends to aggregate. More preferably, it is an acidic region of ⁇ 3.5 to 4.5.
- the chelating agent can use EDTA, ammonia, or the like.
- the chelating agent used in the present invention is not particularly limited as long as the effects of the present invention are exhibited, but is preferably ammonia.
- polycarboxylic acid polyvalent carboxylates, formaldehyde and the like can be used as the reducing agent.
- sodium potassium tartrate Rossiel salt
- glucose glucose
- this reducing agent exhibits weak reducing power and reduces only the oxides (CuO, Cu 0, AgO, Ag O) that are produced as a by-product of the substitution reaction.
- a silver nitrate solution is used as the silver ion solution in the present invention.
- the silver ion solution used in the present invention is not particularly limited as long as the effects of the present invention are exhibited.
- the silver nitrate solution has a silver nitrate concentration of 20 to 300 g / L, preferably 50 to 100 g / L.
- the rate of the silver ion solution added to the copper fine powder slurry is 200 mL / min or less, preferably lOOmL / min or less.
- Decantation treatment is also called the gradient method.
- the solution is allowed to stand to settle copper fine powder or silver-plated copper fine powder, and then the supernatant is gently tilted. Operation to separate and collect. This In this case, since the copper fine powder or silver-plated copper fine powder does not come into contact with the atmosphere, it is possible to proceed to the next step in a state in which re-oxidation of the copper fine powder or silver-plated copper fine powder is prevented.
- One method of post-treatment used in the production method of the present invention is 150 to 220 in a reducing atmosphere under a hydrogen stream.
- C heat treatment for 30-90 minutes.
- C heat treatment is carried out for 20 to 40 minutes, and by this heat treatment, the interface between the copper fine powder and the silver layer is partially alloyed, so that the bond strength at the interface can be increased.
- the silver-plated copper fine powder is kneaded with a resin or solvent when it is made into a conductive paste.
- a resin or solvent when it is made into a conductive paste.
- the silver layer will peel off when subjected to mechanical friction. Therefore, heat treatment at a low temperature in a short time is effective.
- heat treatment is carried out at a very high temperature or for a long time, silver may completely diffuse into copper.
- the second method of post-treatment used in the production method of the present invention is to immerse silver-plated copper fine powder in an alcohol solution containing 0.01 to 5.0% by weight of a fatty acid, and filter after stirring for about 30 minutes. , dry. Preferably, 0.;! ⁇ 1.0 Silver silver fine copper powder is immersed in an alcohol solution containing 10% by weight of fatty acid, filtered and dried after stirring for about 30 minutes. Stearic acid is used as the fatty acid. Fatty acid coating is achieved by the fact that the fatty acid is coated on the surface of the silver-plated copper fine powder to make the surface smooth, and that the fatty acid itself acts as a lubricant to increase the filling ability of the silver-plated copper fine powder. It has an excellent effect.
- the silver-plated copper fine powder and the copper fine powder used in the production method shown above are obtained from ordinary electrolytic methods, reduction methods, atomization methods, mechanical pulverization, etc. with no particular restrictions on the type and production method. It is possible to use the copper fine powder that is used. Further, the shape of the copper powder may be a spherical shape, a flake shape, a needle shape, or a resin shape.
- silver-plated copper fine powder having an average particle size of 1 to 30111, a tap density of 2.4 g / cm 3 or more, and a specific surface area of 0.9 m 2 / g or less can be obtained.
- This silver-plated copper fine powder can further achieve an average particle size of 3 to 20 m, a tap density of 3. Og / cm 3 or more, and a specific surface area of 0.6 m 2 / g or less.
- the silver-plated copper fine powder can be made into a silver-plated copper fine powder having a structure covered with 0.01 to 5.0% by weight of fatty acid by the above treatment. Further, the silver-plated copper fine powder may have a structure coated with 0.;! To 1.0% by weight of fatty acid.
- These silver-plated copper fine powders are useful as conductive pastes.
- the present invention includes a conductive paste manufactured using these copper powders.
- Example 1 electrolytic copper powder obtained by a method called a so-called electrolytic process was used, and copper fine powder obtained by further pulverizing with a jet mill was used.
- This copper fine powder had a weight cumulative particle size D of 6.2 111 as measured by a laser diffraction scattering particle size distribution measurement method.
- a dilute sulfuric acid or potassium hydroxide solution was added to the copper slurry to adjust the pH of the copper slurry to 3.5 to 4.5.
- Example 1 500 g of silver-plated copper fine powder prepared in Example 1 was dispersed in 750 ml of a 0.5% ethanolic stearate solution and stirred for 30 minutes. Then, the solution was separated from the stearic acid-coated silver-plated copper metal powder by filtration washing and suction dehydration, and the stearic acid-coated silver-plated copper metal powder was dried at a temperature of 90 ° C. for 2 hours.
- Example 1 500 g of the silver-plated copper fine powder prepared in Example 1 was placed in a tubular furnace and heat-treated at 200 ° C. for 30 minutes in a reducing atmosphere under a hydrogen stream (3.0 to 3.51 / min). The heat treated silver powdered copper fine powder was pulverized in a mortar.
- Example 3 500 g of silver-plated copper fine powder prepared in Example 3 was dispersed in 750 ml of 0.5% ethanol stearate solution and stirred for 30 minutes. Then, the solution was separated from the stearic acid-coated silver-plated copper metal powder by filtration washing and suction dehydration, and the stearic acid-coated silver-plated copper metal powder was dried at a temperature of 90 ° C. for 2 hours.
- Example 1 500 g of the copper fine powder used in Example 1 was added to 2500 ml of 1% sodium potassium tartrate solution and stirred for several minutes. Next, dilute sulfuric acid or potassium hydroxide solution was added to the copper slurry to adjust the pH of the copper slurry to 3.5-5.
- decantation treatment was performed, 3500 ml of pure water was added, and the mixture was stirred for several minutes. After further decantation treatment, 3500 ml of pure water was added and stirred for several minutes. And filtration The silver-plated copper fine powder and the solution were separated by washing and dehydrating by suction, and the silver-plated copper fine powder was dried at a temperature of 90 ° C. for 2 hours.
- the average particle size, specific surface area, apparent density, and tap density of the silver-plated copper fine powder according to the above-described examples were measured.
- the average particle size was determined by the laser diffraction scattering particle size distribution measurement method, and the value of weight cumulative particle size D was adopted.
- the specific surface area was measured by the BET method. Apparent
- the density was measured according to JISZ2504.
- the tap density was measured according to JISZ2512. The results are shown in Table 1.
- Example 1 an average particle diameter of 9.4 ⁇ 111, specific surface area 0. 33m 2 / g, a tap density of 3. 92 g / cm 3, the resistivity became 1 ⁇ 3X 10- 4 ⁇ 'cm .
- Example 2 an average particle diameter of 11. 7 m, specific surface area 0. 24m 2 / g, a tap density of 4. 76 g / cm 3, specific resistance 7. ivy Do and 1 X 10- 5 ⁇ 'cm.
- the average particle size is 13. 8Mie, specific surface area 0. 19 m 2 / g, a tap density of 3. 99 g / cm 3, the resistivity became 1. 1 X 10- 4 ⁇ 'cm .
- Example 4 the average particle size was 13.3 ⁇ m, the specific surface area was 0.16 m 2 / g, the tap density was 4.95 g / cm 3 , and the specific resistance was 6.5 ⁇ 10 ⁇ 5 ⁇ ′cm. .
- the silver-plated copper fine powder of the present invention having an average particle size of 1 to 30 111, a tap density of 2.4 g / cm 3 or more, and a specific surface area of 0.9 m 2 / g or less.
- the specific resistance is 1 becomes less 5 X 10- 4 ⁇ 'cm, as compared with the comparative example of the raw material powder and below, and shows the good conductivity.
- Example 2 11.7 0.24 3.93 4.76 7.1X10-5
- Example 3 13.8 0.19 2.79 3.99 1.lXlO- 4
- Example 4 13.3 0.16 4.34 4.95 6.5X10-5 Comparative Example 8.7 0.44 2.87 4.00
- the average particle size of Comparative Example 1 is 8.7 m
- the tap density is 4,000 gg / cm 3
- the force specific surface area is 0.44 m 2 / g, compared with the other examples.
- the silver-plated copper fine powder surface has many irregularities, the color tone of the silver-plated surface is poor, and the conductivity is lowered, so that the object of the present invention cannot be achieved, resulting in an undesirable result.
- the silver-plated copper fine powder in which the silver layer is uniformly coated on the surface of the copper fine powder according to the present invention has excellent conductivity.
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Abstract
Description
明 細 書 Specification
銀メツキ銅微粉及び銀メツキ銅微粉を用いて製造した導電ペースト並びに 銀メツキ銅微粉の製造方法 Silver-plated copper fine powder, conductive paste produced using silver-plated copper fine powder, and method for producing silver-plated copper fine powder
技術分野 Technical field
[0001] 本発明は銀メツキ銅微粉及び銀メツキ銅微粉を用いて製造した導電ペースト並び に銀メツキ銅微粉の製造方法に関するものであり、特に導電性と銀メツキ反応時の再 現性に優れ、原料銅微粉並みのタップ密度を有する銀メツキ銅微粉に関する。 [0001] The present invention relates to a silver-plated copper fine powder, a conductive paste produced using the silver-plated copper fine powder, and a method for producing the silver-plated copper fine powder, and is particularly excellent in conductivity and reproducibility during the silver-plated reaction. The present invention relates to a silver-plated copper fine powder having a tap density comparable to that of the raw material copper fine powder.
背景技術 Background art
[0002] 従来、銅微粉は導電ペーストの原料として広く用いられてきた。導電ペーストは、そ の取り极レ、の容易さ故に、実験目的なものから電子産業用途に到るまで広範に使用 されている。 Conventionally, copper fine powder has been widely used as a raw material for conductive paste. Conductive pastes are widely used from experimental purposes to applications in the electronics industry because of their ease of contact.
[0003] なかでも、銀層を表面に被覆した銀メツキ銅微粉は、導電ペーストに加工され、スク リーン印刷法を用いたプリント配線板の回路形成、各種電気的接点部等に応用され 、電気的導通確保の材料として用いられてきた。 In particular, silver-plated copper fine powder with a silver layer coated on its surface is processed into a conductive paste and applied to circuit formation of printed wiring boards using a screen printing method, various electrical contact portions, etc. It has been used as a material for ensuring electrical continuity.
これは、表面に銀層を被覆しない通常の銅微粉と比較したとき、銀メツキ銅微粉は 銅微粉よりも電気的導電性に優れるからである。また、銀粉のみでは高価になるが、 銅に銀をめつきすれば、導電性粉末全体としては安価になり、製造コストを大幅に低 減できる力、らである。したがって、導電特性により優れている銀をメツキした銅微粉か らなる導電ペーストは、低抵抗の導体を低コストで製造できるとレ、う大きなメリットが得 られる。 This is because the silver-plated copper fine powder is more excellent in electrical conductivity than the copper fine powder when compared with normal copper fine powder that does not cover the surface with a silver layer. In addition, silver powder alone is expensive, but if silver is attached to copper, the conductive powder as a whole will be inexpensive and the production cost can be greatly reduced. Therefore, a conductive paste made of fine copper powder coated with silver, which is superior in conductive properties, has a great advantage if a low-resistance conductor can be manufactured at low cost.
[0004] ところで、このような導電ペースト用の銀メツキ銅微粉は、一般的に銅と銀との置換 反応を利用した無電解置換メツキ法により製造する技術が知られている。特許文献 1 には、硝酸銀、炭酸アンモニゥム塩、エチレンジァミン四酢酸塩の銀錯塩溶液を用い て金属銅粉の表面に銀を置換析出させる方法についての記載がある。 [0004] By the way, a technique for producing such a silver-plated copper fine powder for a conductive paste is generally known by an electroless substitution plating method using a substitution reaction between copper and silver. Patent Document 1 describes a method of substituting and depositing silver on the surface of metallic copper powder using a silver complex solution of silver nitrate, ammonium carbonate, and ethylenediamine tetraacetate.
また、特許文献 2には、キレート化剤溶液に銅粉を分散し、該銅粉分散液に硝酸銀 溶液を加え、次レ、で還元剤を添加して銅粉表面へ銀被膜を析出させる方法が開示さ れている。 さらに、特許文献 3には、銅粉分散液にキレート化剤を加えて銅粉スラリーを作製し 、これに緩衝剤を添加して pH調整を行い、これに銀イオンを添加して置換反応によ り銀コート銅粉とする技術が開示されている。 Patent Document 2 discloses a method in which copper powder is dispersed in a chelating agent solution, a silver nitrate solution is added to the copper powder dispersion, a reducing agent is added in the next step, and a silver film is deposited on the surface of the copper powder. Is disclosed. Furthermore, in Patent Document 3, a chelating agent is added to a copper powder dispersion to prepare a copper powder slurry, and a buffer is added thereto to adjust pH, and then silver ions are added to this for a substitution reaction. A technique for making silver-coated copper powder is disclosed.
[0005] これらの製造方法で得られる銀メツキ銅微粉は、導電性や耐湿性の特性に優れ、 導電ペースト材料としては好適な材料として利用されてきた。しかし、これらの製造方 法で得られた銀メツキ銅微粉は、銀メツキ前の銅微粉の酸化状態によって銀メツキ反 応後の色調にバラツキが生じることや、銀メツキによるタップ密度の低下等の問題点 を抱えていた。 [0005] The silver-plated copper fine powder obtained by these production methods is excellent in electrical conductivity and moisture resistance, and has been used as a suitable material as a conductive paste material. However, the silver-plated copper fine powders obtained by these manufacturing methods have variations in the color tone after the silver-plated reaction due to the oxidation state of the copper fine powder before the silver-plated, and the tap density is reduced by the silver-plated, etc. I had a problem.
特許文献 1 :特開昭 57— 59283号公報 Patent Document 1: JP-A-57-59283
特許文献 2:特開平 2— 46641号公報 Patent Document 2: JP-A-2-46641
特許文献 2:特開 2004— 52044号公報 Patent Document 2: JP 2004-52044 A
発明の開示 Disclosure of the invention
発明が解決しょうとする課題 Problems to be solved by the invention
[0006] 本発明は、上記の問題点を解決することを目的とし、導電性と銀メツキ反応時の再 現性に優れ、原料銅微粉並みのタップ密度を有する銀メツキ銅微粉及びその製造方 法を提供する。 [0006] The present invention aims to solve the above-described problems, and is a silver-plated copper fine powder having excellent conductivity and reproducibility during a silver-plated reaction, and having a tap density similar to that of the raw copper fine powder, and a method for producing the same. Provide law.
課題を解決するための手段 Means for solving the problem
[0007] 本発明者等は、上記課題を解決するために鋭意研究した結果、従来の銀メツキ銅 微粉において銀メツキ反応の前後に表面処理工程を導入すること及び無電解置換メ ツキと還元型メツキにより銅微粉表面に銀層を形成することで、銀メツキ製造時の再現 性に優れ、原料銅微粉並みのタップ密度を有する銀メツキ銅微粉となることを見出し た。 [0007] As a result of diligent research to solve the above problems, the present inventors have introduced a surface treatment step before and after the silver plating reaction in the conventional silver plating copper fine powder, and electroless substitution plating and reduction type. By forming a silver layer on the surface of the copper fine powder by plating, it was found that the silver-plated copper fine powder was excellent in reproducibility during the production of silver plating and had a tap density similar to that of the raw copper powder.
[0008] これらの知見に基づき、本発明は [0008] Based on these findings, the present invention
1)平均粒径が;!〜 30 111、タップ密度が 2. 4g/cm3以上、比表面積が 0. 9m2/g 以下である銀メツキ銅微粉 1) Silver-plated copper fine powder with average particle size;! ~ 30 111, tap density 2.4 g / cm 3 or more, specific surface area 0.9 m 2 / g or less
2)平均粒径が3〜20 111、タップ密度が 3. Og/cm3以上、比表面積が 0. 6m g 以下である銀メツキ銅微粉 2) Silver-plated copper fine powder with an average particle size of 3 to 20 111, tap density of 3. Og / cm 3 or more, and specific surface area of 0.6 mg or less
3)銀メツキ銅微粉が、さらに 0. 0;!〜 5. 0重量%の脂肪酸で被覆されている上記 1又 は 2記載の銀メツキ銅微粉 3) The above 1 or 2 above, wherein the silver-plated copper fine powder is further coated with 0.0%;! To 5.0% by weight of fatty acid. Is the silver-plated copper fine powder described in 2.
4)銀メツキ銅微粉が、さらに 0. ;!〜 1. 0重量%の脂肪酸で被覆されている上記 1又 は 2記載の銀メツキ銅微粉 4) The silver-plated copper fine powder according to 1 or 2 above, wherein the silver-plated copper fine powder is further coated with 0.;!-1.0% by weight of fatty acid.
5)上記 1〜4のいずれかに記載の銀メツキ銅微粉を用いて製造した導電ペースト、を 提供する。 5) Provided is a conductive paste produced using the silver-plated copper fine powder according to any one of 1 to 4 above.
本発明は、また The present invention also provides
6)銅微粉の表面に銀層を形成する銀メツキ銅微粉の製造方法において、銅微粉を アルカリ性溶液中で銅微粉表面の有機物を除去 ·水洗し、次に酸性溶液中で銅微粉 表面の酸化物を酸洗,水洗した後、この銅微粉を分散させた酸性溶液中に還元剤を 添加し pHを調整して銅微粉スラリーを作成し、この銅微粉スラリーに銀イオン溶液を 連続的に添加することにより、無電解置換メツキと還元型無電解メツキにより銅微粉表 面に銀層を形成する銀メツキ銅微粉の製造方法 6) In the silver-plated copper fine powder manufacturing method that forms a silver layer on the surface of the copper fine powder, remove the copper fine powder from the organic matter on the surface of the copper fine powder in an alkaline solution. After pickling and washing the product, a reducing agent is added to the acidic solution in which the copper fine powder is dispersed to adjust the pH to create a copper fine powder slurry, and a silver ion solution is continuously added to the copper fine powder slurry. A method for producing silver-plated copper fine powder in which a silver layer is formed on the surface of the copper fine powder by electroless replacement plating and reduced electroless plating.
7)前記アルカリ性溶液として水酸化カリウムを用い、酸性溶液として硫酸を用いること を特徴とする上記 6記載の銀メツキ銅微粉の製造方法 7) The method for producing silver-plated copper fine powder according to 6 above, wherein potassium hydroxide is used as the alkaline solution and sulfuric acid is used as the acidic solution.
8)還元剤として多価カルボン酸若しくはその塩類又はホルムアルデヒドから選択した 1種又は 2種以上を用いる上記 6又は 7記載の銀メツキ銅微粉の製造方法 8) The method for producing a silver-plated copper fine powder according to 6 or 7 above, wherein one or more selected from polyvalent carboxylic acids or salts thereof or formaldehyde are used as the reducing agent
9)銀イオン溶液添加開始時の pHを 3· 0〜5. 0に調整する上記 6〜8のいずれかに 記載の銀メツキ銅微粉の製造方法 9) The method for producing a silver-plated copper fine powder according to any one of the above 6 to 8, wherein the pH at the start of addition of the silver ion solution is adjusted to 3.0 to 5.0
10)銀イオン溶液添加開始時の pHを 3· 5〜4. 5に調整する上記 6〜8のいずれか に記載の銀メツキ銅微粉の製造方法 10) The method for producing a silver-plated copper fine powder according to any one of 6 to 8 above, wherein the pH at the start of addition of the silver ion solution is adjusted to 3.5 to 4.5.
11)銀イオン溶液は、透明なアンモニア性硝酸銀溶液である上記 6〜; 10のいずれか に記載の銀メツキ銅微粉の製造方法 11) The method for producing a silver-plated copper fine powder according to any one of 6 to 10 above, wherein the silver ion solution is a transparent ammoniacal silver nitrate solution.
12)銀メツキ銅微粉を水素気流下の還元性雰囲気中で 150〜220° C、 20〜90分 間、熱処理を行う上記 6〜; 11の!/、ずれかに記載の銀メツキ銅微粉の製造方法 12) The silver-plated copper fine powder according to any one of 6 to 11 above, wherein the silver-plated copper fine powder is heat-treated in a reducing atmosphere under a hydrogen stream at 150 to 220 ° C. for 20 to 90 minutes. Production method
13)銀メツキ銅微粉を水素気流下の還元性雰囲気中で 180〜210° C、 20〜40分 間、熱処理を行う上記 6〜; 11の!/、ずれかに記載の銀メツキ銅微粉の製造方法13) The silver-plated copper fine powder according to any one of 6 to 11 above, wherein the silver-plated copper fine powder is heat-treated in a reducing atmosphere under a hydrogen stream at 180 to 210 ° C. for 20 to 40 minutes. Production method
14)銀メツキ銅微粉を、脂肪酸を含むアルコール溶液中に浸漬し、銀メツキ銅微粉の 表面を 0. 01 -5. 0重量%の脂肪酸で被覆する上記 6〜; 13のいずれかに記載の銀 メツキ銅微粉の製造方法 14) The silver plating copper fine powder is immersed in an alcohol solution containing a fatty acid, and the surface of the silver plating copper fine powder is coated with 0.01 to 5.0 wt% of fatty acid. Silver Method for producing fine copper powder
15)銀メツキ銅微粉を、脂肪酸を含むアルコール溶液中に浸漬し、銀メツキ銅微粉の 表面を 0.;!〜 1. 0重量%の脂肪酸で被覆する上記 6〜; 13のいずれかに記載の銀メ ツキ銅微粉の製造方法、を提供するものである。 15) The silver plating copper fine powder is immersed in an alcohol solution containing a fatty acid, and the surface of the silver plating copper fine powder is coated with 0.;! To 1.0% by weight of fatty acid. A method for producing a silver-plated copper fine powder.
発明の効果 The invention's effect
[0010] 銀メツキ反応の前後に表面処理工程を導入すること及び無電解置換メツキと還元型 メツキにより銅微粉表面に銀層を形成することで、銅微粉表面に銀層を均一に被覆 することが可能となり、その結果、優れた導電性を有するとともに銀メツキ反応時の再 現性に優れ、原料銅微粉並みのタップ密度を有する銀メツキ銅微粉となり、導電ぺー ストに使用した際に安定的に高充填化を達成することができるという優れた効果を有 する。 [0010] The surface of the copper fine powder is uniformly coated by introducing a surface treatment step before and after the silver plating reaction and forming a silver layer on the surface of the copper fine powder by electroless substitution plating and reduction type plating. As a result, it has excellent conductivity and reproducibility at the time of silver plating reaction, resulting in silver plating copper fine powder with tap density comparable to that of raw copper fine powder, which is stable when used in conductive paste. In addition, it has an excellent effect that high filling can be achieved.
発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION
[0011] 従来は、酸性溶液でなくアルカリ性溶液を使用するため、粉として取り出す際に銅 水酸化物が再沈殿してしまうおそれがあった。また、置換反応の際、銀イオン溶液を まとめて投入するため、銀イオン濃度が銅粉周辺で不均一になり、銀の被覆状態の 悪い銀メツキ銅微粉が形成されることが考えられた。 [0011] Conventionally, since an alkaline solution is used instead of an acidic solution, the copper hydroxide may be re-precipitated when taken out as a powder. In addition, since the silver ion solution was charged all together during the substitution reaction, it was considered that the silver ion concentration became non-uniform around the copper powder, and silver-plated copper fine powder with poor silver coating was formed.
これに対し本発明は、アルカリ性溶液中に銅微粉を分散させることで銅微粉表面の 有機物を除去し、酸性溶液中に銅微粉を分散させることで銅微粉表面の酸化物を除 去し、キレート化剤により錯体化した銅イオンを安定な状態で維持できるように pH調 整をし、銀イオンとの置換反応が均一的に進行するように銀イオン溶液を連続的に添 カロしているため、銅微粉表面に極めて均一に銀層を被覆できる。 In contrast, the present invention removes the organic matter on the surface of the copper fine powder by dispersing the copper fine powder in the alkaline solution, and removes the oxide on the surface of the copper fine powder by dispersing the copper fine powder in the acidic solution. The pH is adjusted so that the copper ions complexed by the agent can be maintained in a stable state, and the silver ion solution is continuously added so that the substitution reaction with silver ions proceeds uniformly. The silver layer can be coated extremely uniformly on the surface of the copper fine powder.
[0012] アルカリ性溶液として、水酸化ナトリウム、水酸化カリウム等を用いる。置換反応させ る前に銅微粉表面の有機物を確実に除去できるアルカリ性溶液であればょレ、が、好 ましくは水酸化カリウムとする。 [0012] Sodium hydroxide, potassium hydroxide, or the like is used as the alkaline solution. An alkaline solution that can reliably remove the organic matter on the surface of the copper fine powder before the substitution reaction is preferred, but potassium hydroxide is preferred.
酸性溶液にあっては、硫酸、塩酸、リン酸等を用いる。好ましくは硫酸とし、置換反 応をさせる前に銅微粉表面の銅酸化物を確実に除去できる酸性溶液であればよい 力、その選択する種類や濃度は過剰に銅微粉の銅自体を溶解しないようにする必要 力 sある。 この酸性溶液の pHは 2· 0〜5· 0の酸性領域とすることが望ましい。 ρΗが 5. 0を越 えると銅微粉の酸化物を十分に溶解除去できなくなり、 pHが 2. 0より小さくなると銅 粉の溶解が生じ、銅微粉自体の凝集も進行し易くなる。より好ましくは、 ρΗ3. 5〜4. 5の酸性領域である。 In an acidic solution, sulfuric acid, hydrochloric acid, phosphoric acid or the like is used. It is preferable to use sulfuric acid, and it should be an acidic solution that can reliably remove the copper oxide on the surface of the copper fine powder before the substitution reaction. The selected type and concentration should not excessively dissolve the copper fine copper itself. there is a need force s to. The pH of this acidic solution is preferably in the acidic range of 2 · 0 to 5 · 0. When ρΗ exceeds 5.0, oxides of copper fine powder cannot be sufficiently dissolved and removed, and when pH is lower than 2.0, copper powder dissolves and the copper fine powder itself tends to aggregate. More preferably, it is an acidic region of ρΗ3.5 to 4.5.
[0013] また、本発明の製造方法において、キレート化剤は EDTAやアンモニア等を用いる こと力 Sできる。本発明で用いられるキレート化剤は、本発明の効果を奏する限り、特に 制限されるものではないが、好ましくはアンモニアとする。 [0013] In the production method of the present invention, the chelating agent can use EDTA, ammonia, or the like. The chelating agent used in the present invention is not particularly limited as long as the effects of the present invention are exhibited, but is preferably ammonia.
硝酸銀溶液にアンモニア水を加えると、沈殿を生じるが、過剰のアンモニア水を加 えると、透明なアンモニア性硝酸銀溶液 (この中に [Ag (NH ) ] +を含む)が得られる Addition of ammonia water to silver nitrate solution causes precipitation, but addition of excess ammonia water gives a clear ammoniacal silver nitrate solution (with [Ag (NH)] + in it)
3 2 3 2
。これに酒石酸ナトリウムカリウムなどの還元剤を加えると銅微粉の表面に銀が析出し 、銀メツキ銅微粉が形成される。 . When a reducing agent such as sodium potassium tartrate is added thereto, silver is deposited on the surface of the copper fine powder, and silver-plated copper fine powder is formed.
[0014] また、本発明にお!/、て還元剤は、多価カルボン酸、多価カルボン酸塩類、ホルムァ ルデヒド等を用いることができる。例えば、酒石酸ナトリウムカリウム(ロッシエル塩)や ブドウ糖 (グルコース)などが挙げられる。好ましくは、酒石酸ナトリウムカリウム(ロッシ エル塩)とし、この還元剤は弱い還元力を示し、置換反応の副生物として生成する酸 化物(CuO、 Cu 0、 AgO、 Ag O)のみを還元し、銅の錯イオンまでは還元させない [0014] In the present invention, polycarboxylic acid, polyvalent carboxylates, formaldehyde and the like can be used as the reducing agent. For example, sodium potassium tartrate (Rosiel salt) and glucose (glucose). Preferably, it is sodium potassium tartrate (Roschel's salt), and this reducing agent exhibits weak reducing power and reduces only the oxides (CuO, Cu 0, AgO, Ag O) that are produced as a by-product of the substitution reaction. The complex ion of
2 2 twenty two
〇 Yes
[0015] そして、本発明における銀イオン溶液は硝酸銀溶液を用いる。本発明で用いられる 銀イオン溶液は、本発明の効果を奏する限り、特に制限はされない。この硝酸銀溶 液は硝酸銀濃度 20〜300g/Lとし、好ましくは 50〜; 100g/Lとする。 [0015] A silver nitrate solution is used as the silver ion solution in the present invention. The silver ion solution used in the present invention is not particularly limited as long as the effects of the present invention are exhibited. The silver nitrate solution has a silver nitrate concentration of 20 to 300 g / L, preferably 50 to 100 g / L.
また、銅微粉スラリーに添加する銀イオン溶液の速度は、 200mL/min以下とし、 好ましくは lOOmL/min以下とする。上記濃度範囲の硝酸銀溶液を比較的ゆっくり とした添加速度、実用的には 20〜200mL/minで添加することで、銅微粉表面に 均一な銀層を被覆することが確実に行うことができる。 The rate of the silver ion solution added to the copper fine powder slurry is 200 mL / min or less, preferably lOOmL / min or less. By adding a silver nitrate solution in the above concentration range at a relatively slow rate, practically 20 to 200 mL / min, a uniform silver layer can be reliably coated on the copper fine powder surface.
[0016] さらに、本発明の製造方法において、酸性溶液中に銅微粉を分散した後、デカン テーシヨン処理を行うことが好ましい。デカンテーシヨン処理は、傾斜法とも呼ばれ、 酸性溶液に銅微粉を分散させた後、溶液を静置することで銅微粉もしくは銀メツキ銅 微粉を沈降させた後、上澄み液を静かに傾斜して分離採取する操作をいう。これによ れば、銅微粉もしくは銀メツキ銅微粉が大気と接触することがないので、銅微粉もしく は銀メツキ銅微粉の再酸化を防止した状態で次工程に移行することが可能となる。 [0016] Further, in the production method of the present invention, it is preferable to carry out a decantation treatment after the copper fine powder is dispersed in the acidic solution. Decantation treatment is also called the gradient method. After copper fine powder is dispersed in an acidic solution, the solution is allowed to stand to settle copper fine powder or silver-plated copper fine powder, and then the supernatant is gently tilted. Operation to separate and collect. This In this case, since the copper fine powder or silver-plated copper fine powder does not come into contact with the atmosphere, it is possible to proceed to the next step in a state in which re-oxidation of the copper fine powder or silver-plated copper fine powder is prevented.
[0017] 本発明の製造方法に用いる後処理の 1の方法は、水素気流下の還元性雰囲気中 で 150〜220。 C、 30〜90分間で熱処理を行う。好ましくは 180〜210。 C、 20〜4 0分間で熱処理を行い、この熱処理により銅微粉と銀層の界面を一部合金化すること で、界面の結合力を高めることができる。 [0017] One method of post-treatment used in the production method of the present invention is 150 to 220 in a reducing atmosphere under a hydrogen stream. C, heat treatment for 30-90 minutes. Preferably 180-210. C, heat treatment is carried out for 20 to 40 minutes, and by this heat treatment, the interface between the copper fine powder and the silver layer is partially alloyed, so that the bond strength at the interface can be increased.
銀メツキ銅微粉は導電性ペーストとする際に、樹脂や溶剤と混合して混練りするが、 界面の結合力が弱いと、機械的摩擦を受けた時に銀層の剥離が生じてしまう。そこで 、低温短時間での熱処理が有効となる。ただし、熱処理をあまり高温下や長時間行う と銀が銅に完全に拡散してしまう虞がある。 The silver-plated copper fine powder is kneaded with a resin or solvent when it is made into a conductive paste. However, if the bonding force at the interface is weak, the silver layer will peel off when subjected to mechanical friction. Therefore, heat treatment at a low temperature in a short time is effective. However, if heat treatment is carried out at a very high temperature or for a long time, silver may completely diffuse into copper.
[0018] 本発明の製造方法に用いる後処理の 2の方法は、 0. 01 -5. 0重量%の脂肪酸を 含むアルコール溶液中に銀メツキ銅微粉を浸漬し、 30分間程度の攪拌後に濾過、 乾燥する。好ましくは、 0. ;!〜 1. 0重量%の脂肪酸を含むアルコール溶液中に銀メッ キ銅微粉を浸漬し、 30分程度の攪拌後に濾過、乾燥する。脂肪酸はステアリン酸を 用いる。脂肪酸被覆は、脂肪酸が銀メツキ銅微粉表面の凹凸に被覆されることにより 表面が平滑化されることや脂肪酸自体が潤滑剤の役割を果たし銀メツキ銅微粉の充 填性が高まることとレ、う優れた効果を有する。 [0018] The second method of post-treatment used in the production method of the present invention is to immerse silver-plated copper fine powder in an alcohol solution containing 0.01 to 5.0% by weight of a fatty acid, and filter after stirring for about 30 minutes. , dry. Preferably, 0.;! ~ 1.0 Silver silver fine copper powder is immersed in an alcohol solution containing 10% by weight of fatty acid, filtered and dried after stirring for about 30 minutes. Stearic acid is used as the fatty acid. Fatty acid coating is achieved by the fact that the fatty acid is coated on the surface of the silver-plated copper fine powder to make the surface smooth, and that the fatty acid itself acts as a lubricant to increase the filling ability of the silver-plated copper fine powder. It has an excellent effect.
これら後処理により銀メツキ反応により低下した銀メツキ銅微粉のタップ密度を原料 銅微粉並みに高めることができ、高充填性を要求されるビアホール用途で有利となる のである。 These post-treatments can increase the tap density of the silver-plated copper fine powder, which has been lowered by the silver-plated reaction, to the same level as the raw copper powder, which is advantageous for via-hole applications that require high fillability.
[0019] 上記に示した銀メツキ銅微粉及びその製造方法に用いられる銅微粉は、その種類 、製法等に特に制限がなぐ通常の電解法、還元法、アトマイズ法、機械的粉砕等か ら得られる銅微粉が用いること力 Sできる。また、その銅粉形状も特定はなぐ球状、フ レーク状、針状、樹脂状のものを用いることができる。 [0019] The silver-plated copper fine powder and the copper fine powder used in the production method shown above are obtained from ordinary electrolytic methods, reduction methods, atomization methods, mechanical pulverization, etc. with no particular restrictions on the type and production method. It is possible to use the copper fine powder that is used. Further, the shape of the copper powder may be a spherical shape, a flake shape, a needle shape, or a resin shape.
以上によって、平均粒径が1〜30 111、タップ密度が 2. 4g/cm3以上、比表面積 が 0. 9m2/g以下である銀メツキ銅微粉を得ることができる。この銀メツキ銅微粉は、 さらに平均粒径が 3〜20 m、タップ密度が 3. Og/cm3以上、比表面積が 0. 6m2 /g以下を達成することができる。 また、この銀メツキ銅微粉は、上記の処理により 0. 01 -5. 0重量%の脂肪酸で被 覆された構造の銀メツキ銅微粉とすることができる。さらに、この銀メツキ銅微粉は、 0 . ;!〜 1. 0重量%の脂肪酸で被覆された構造とすることもできる。これらの銀メツキ銅 微粉は導電ペーストとして有用である。本願発明は、これらの銅粉をもちいて製造し た導電性ペーストを含むものである。 As described above, silver-plated copper fine powder having an average particle size of 1 to 30111, a tap density of 2.4 g / cm 3 or more, and a specific surface area of 0.9 m 2 / g or less can be obtained. This silver-plated copper fine powder can further achieve an average particle size of 3 to 20 m, a tap density of 3. Og / cm 3 or more, and a specific surface area of 0.6 m 2 / g or less. Further, the silver-plated copper fine powder can be made into a silver-plated copper fine powder having a structure covered with 0.01 to 5.0% by weight of fatty acid by the above treatment. Further, the silver-plated copper fine powder may have a structure coated with 0.;! To 1.0% by weight of fatty acid. These silver-plated copper fine powders are useful as conductive pastes. The present invention includes a conductive paste manufactured using these copper powders.
実施例 Example
[0020] 次に実施例に基づいて本発明を説明する。以下に示す実施例は、本発明の理解 を容易にするためのものであり、これらの実施例よつて本発明を制限するものではな い。すなわち、本発明の技術思想に基づく変形及び他の実施例は、本発明に含まれ るものである。 Next, the present invention will be described based on examples. The following examples are for facilitating the understanding of the present invention, and the present invention is not limited by these examples. That is, modifications and other examples based on the technical idea of the present invention are included in the present invention.
[0021] (実施例 1) [Example 1]
本実施例 1にお!/、ては、 V、わゆる電解法と呼ばれる製法により得られた電解銅粉を 、さらにジェットミルで粉砕して得られた銅微粉を使用した。この銅微粉はレーザー回 折散乱式粒度分布測定法による重量累積粒径 D は 6. 2 111であった。 In Example 1,! /, V, electrolytic copper powder obtained by a method called a so-called electrolytic process was used, and copper fine powder obtained by further pulverizing with a jet mill was used. This copper fine powder had a weight cumulative particle size D of 6.2 111 as measured by a laser diffraction scattering particle size distribution measurement method.
50 50
この銅微粉 500gを 1 %水酸化カリウム水溶液 1000mlに加えて 20分間攪拌し、続 いて一次デカンテーシヨン処理を行い、さらに純水 1000mlを加えて数分間攪拌した 500 g of this copper fine powder was added to 1000 ml of 1% aqueous potassium hydroxide solution and stirred for 20 minutes, followed by primary decantation treatment, and further 1000 ml of pure water was added and stirred for several minutes.
〇 Yes
その後、二次デカンテーシヨン処理を行い、硫酸濃度 15g/Lの硫酸水溶液 2500 mlを加えて 30分間攪拌した。さらに、三次デカンテーシヨン処理を行い、純水 2500 mlを加えて数分間攪拌した。 Thereafter, secondary decantation treatment was performed, and 2500 ml of sulfuric acid aqueous solution having a sulfuric acid concentration of 15 g / L was added and stirred for 30 minutes. Further, tertiary decantation treatment was performed, 2500 ml of pure water was added, and the mixture was stirred for several minutes.
次いで、四次デカンテーシヨン処理を行い、 1 %酒石酸ナトリウムカリウム溶液 2500 mlを加えて数分間攪拌し、銅スラリーを形成させた。 Next, quaternary decantation treatment was performed, 2500 ml of a 1% sodium potassium tartrate solution was added and stirred for several minutes to form a copper slurry.
該銅スラリーに希硫酸又は水酸化カリウム溶液を加えて、銅スラリーの pHを 3· 5〜 4. 5になるように調整した。 A dilute sulfuric acid or potassium hydroxide solution was added to the copper slurry to adjust the pH of the copper slurry to 3.5 to 4.5.
[0022] pHを調整した銅スラリーに硝酸銀アンモニア溶液 1000ml (硝酸銀 887· 5gを水に 添加してアンモニア水を加え、 1000mlとして調整したもの)を、 30分間の時間をかけ てゆっくりと添加しながら置換反応処理及び還元反応処理を行い、さらに 30分間の 攪拌をして銀メツキ銅微粉を得た。 その後、五次デカンテーシヨン処理を行い、純水 3500mlを加えて数分間攪拌した 。さらに六次デカンテーシヨン処理を行い、純水 3500mlを加えて数分間攪拌した。 そして、濾過洗浄、吸引脱水することで銀メツキ銅微粉と溶液とを濾別し、銀メツキ銅 微粉を 90° Cの温度で 2時間の乾燥を行った。 [0022] To a copper slurry adjusted in pH, 1000 ml of a silver nitrate ammonia solution (a mixture of 887 · 5 g of silver nitrate and water added to adjust the water to 1000 ml) was slowly added over a period of 30 minutes. Substitution reaction treatment and reduction reaction treatment were performed, and stirring was further performed for 30 minutes to obtain a silver-plated copper fine powder. Thereafter, a fifth decantation treatment was performed, 3500 ml of pure water was added, and the mixture was stirred for several minutes. Further, a sixth decantation treatment was performed, 3500 ml of pure water was added, and the mixture was stirred for several minutes. Then, the silver-plated copper fine powder and the solution were separated by filtration and suction dehydration, and the silver-plated copper fine powder was dried at a temperature of 90 ° C. for 2 hours.
[0023] (実施例 2) [0023] (Example 2)
実施例 1で作製した銀メツキ銅微粉 500gを 0. 5%ステアリン酸エタノール溶液 750 mlに分散させ、 30分間攪拌した。そして、濾過洗浄、吸引脱水することでステアリン 酸被覆銀メツキ銅微粉と溶液とを濾別し、ステアリン酸被覆銀メツキ銅微粉を 90° C の温度で 2時間の乾燥を行った。 500 g of silver-plated copper fine powder prepared in Example 1 was dispersed in 750 ml of a 0.5% ethanolic stearate solution and stirred for 30 minutes. Then, the solution was separated from the stearic acid-coated silver-plated copper metal powder by filtration washing and suction dehydration, and the stearic acid-coated silver-plated copper metal powder was dried at a temperature of 90 ° C. for 2 hours.
[0024] (実施例 3) [0024] (Example 3)
実施例 1で作製した銀メツキ銅微粉 500gを管状炉に入れ、水素気流下(3. 0〜3. 51/min)の還元性雰囲気中で 200° C、 30分間熱処理した。熱処理済みの銀メッ キ銅微粉を乳鉢で粉砕した。 500 g of the silver-plated copper fine powder prepared in Example 1 was placed in a tubular furnace and heat-treated at 200 ° C. for 30 minutes in a reducing atmosphere under a hydrogen stream (3.0 to 3.51 / min). The heat treated silver powdered copper fine powder was pulverized in a mortar.
[0025] (実施例 4) [Example 4]
実施例 3で作製した銀メツキ銅微粉 500gを 0. 5%ステアリン酸エタノール溶液 750 mlに分散させ、 30分間攪拌した。そして、濾過洗浄、吸引脱水することでステアリン 酸被覆銀メツキ銅微粉と溶液とを濾別し、ステアリン酸被覆銀メツキ銅微粉を 90° C の温度で 2時間の乾燥を行った。 500 g of silver-plated copper fine powder prepared in Example 3 was dispersed in 750 ml of 0.5% ethanol stearate solution and stirred for 30 minutes. Then, the solution was separated from the stearic acid-coated silver-plated copper metal powder by filtration washing and suction dehydration, and the stearic acid-coated silver-plated copper metal powder was dried at a temperature of 90 ° C. for 2 hours.
[0026] (比較例 1) [Comparative Example 1]
1 %酒石酸ナトリウムカリウム溶液 2500mlに実施例 1で使用した銅微粉 500gを加 えて数分間攪拌した。次に銅スラリーに希硫酸又は水酸化カリウム溶液を加えて、銅 スラリーの pHを 3· 5〜4· 5に調整した。 500 g of the copper fine powder used in Example 1 was added to 2500 ml of 1% sodium potassium tartrate solution and stirred for several minutes. Next, dilute sulfuric acid or potassium hydroxide solution was added to the copper slurry to adjust the pH of the copper slurry to 3.5-5.
このように ρΗ調整した銅スラリーに硝酸銀アンモユア溶液 1000ml (硝酸銀 87· 5g を水に添加してアンモニア水を加え、 1000mlとして調整したもの)を、 30分間の時間 をかけてゆっくりと添加しながら置換反応処理及び還元反応処理を行い、さらに 30 分間の攪拌をして銀メツキ銅微粉を得た。 In this way, 1000 ml of silver nitrate ammonia solution (adjusted to 1000 ml of silver nitrate by adding 85.5 g of silver nitrate to water and adjusted to 1000 ml) was added to the copper slurry adjusted to ρΗ while slowly adding over 30 minutes. A reaction treatment and a reduction reaction treatment were performed, and stirring was further performed for 30 minutes to obtain a silver-plated copper fine powder.
続いてデカンテーシヨン処理を行い、純水 3500mlを加えて数分間攪拌した。さらに デカンテーシヨン処理を行い、純水 3500mlを加えて数分間攪拌した。そして、濾過 洗浄、吸引脱水することで銀メツキ銅微粉と溶液とを濾別し、銀メツキ銅微粉を 90° Cの温度で 2時間の乾燥を行った。 Subsequently, decantation treatment was performed, 3500 ml of pure water was added, and the mixture was stirred for several minutes. After further decantation treatment, 3500 ml of pure water was added and stirred for several minutes. And filtration The silver-plated copper fine powder and the solution were separated by washing and dehydrating by suction, and the silver-plated copper fine powder was dried at a temperature of 90 ° C. for 2 hours.
[0027] 上述の実施例に係る銀メツキ銅微粉に関し、その平均粒径、比表面積、見掛密度、 及びタップ密度を測定した。平均粒径はレーザー回折散乱式粒度分布測定法による もので、重量累積粒径 D の値を採用した。比表面積は BET法により測定した。見掛 [0027] The average particle size, specific surface area, apparent density, and tap density of the silver-plated copper fine powder according to the above-described examples were measured. The average particle size was determined by the laser diffraction scattering particle size distribution measurement method, and the value of weight cumulative particle size D was adopted. The specific surface area was measured by the BET method. Apparent
50 50
密度は JISZ2504により測定した。タップ密度は JISZ2512により測定した。その結果を 表 1に示す。 The density was measured according to JISZ2504. The tap density was measured according to JISZ2512. The results are shown in Table 1.
この表 1に示すように、原料粉の平均粒径は 6. 2^ 111,比表面積 0. 48m2/g、タツ プ密度 4. 98g/cm3、比抵抗は 2. 9 X 10_4Ω 'cmとなった As shown in Table 1, the average particle diameter of the raw material powder 6.2 ^ 111, specific surface area 0. 48m 2 / g, Tatsu flop density 4. 98 g / cm 3, the resistivity is 2. 9 X 10_ 4 Ω became 'cm
実施例 1では、平均粒径が 9. 4^ 111,比表面積 0. 33m2/g、タップ密度 3. 92g/ cm3、比抵抗は 1· 3X 10— 4Ω 'cmとなった。実施例 2では、平均粒径が 11. 7 m、 比表面積 0. 24m2/g、タップ密度 4. 76g/cm3、比抵抗は 7. 1 X 10— 5Ω 'cmとな つた。実施例 3では、平均粒径が 13. 8μΐη,比表面積 0. 19m2/g、タップ密度 3. 99g/cm3、比抵抗は 1. 1 X 10— 4Ω 'cmとなった。また、実施例 4では、平均粒径が 13. 3〃m、比表面積 0. 16m2/g、タップ密度 4. 95g/cm3、比抵抗は 6. 5X 10— 5 Ω 'cmとなった。 In Example 1, an average particle diameter of 9.4 ^ 111, specific surface area 0. 33m 2 / g, a tap density of 3. 92 g / cm 3, the resistivity became 1 · 3X 10- 4 Ω 'cm . In Example 2, an average particle diameter of 11. 7 m, specific surface area 0. 24m 2 / g, a tap density of 4. 76 g / cm 3, specific resistance 7. ivy Do and 1 X 10- 5 Ω 'cm. In Example 3, the average particle size is 13. 8Mie, specific surface area 0. 19 m 2 / g, a tap density of 3. 99 g / cm 3, the resistivity became 1. 1 X 10- 4 Ω 'cm . In Example 4, the average particle size was 13.3 μm, the specific surface area was 0.16 m 2 / g, the tap density was 4.95 g / cm 3 , and the specific resistance was 6.5 × 10−5 Ω′cm. .
これらはいずれも、平均粒径が1〜30 111、タップ密度が 2. 4g/cm3以上、比表 面積が 0. 9m2/g以下である本願発明の銀メツキ銅微粉の範囲に入るもので、好適 な銀メツキ銅微粉であった。また、実施例 1から実施例 4はいずれも、比抵抗は 1. 5 X 10— 4Ω 'cm以下となり、原料粉及び後述する比較例に比べて、良好な導電性を示 した。 All of these fall within the range of the silver-plated copper fine powder of the present invention having an average particle size of 1 to 30 111, a tap density of 2.4 g / cm 3 or more, and a specific surface area of 0.9 m 2 / g or less. Thus, it was a suitable silver-plated copper fine powder. Moreover, none of the first through fourth embodiments, the specific resistance is 1 becomes less 5 X 10- 4 Ω 'cm, as compared with the comparative example of the raw material powder and below, and shows the good conductivity.
[0028] [表 1] D50 比表面積 見掛密度 夕ップ密度 比抵抗 [0028] [Table 1] D 50 Specific surface area Apparent density Yupp density Resistivity
(,μ m) (mVg) (g/cm3) (g/cm3) (, μ m) (mVg) (g / cm 3 ) (g / cm 3 )
原料粉 6.2 0.48 3.69 4.98 2.9X10"4 実施例 1 9.4 0.33 3.13 3.92 Raw material powder 6.2 0.48 3.69 4.98 2.9X10 " 4 Example 1 9.4 0.33 3.13 3.92
実施例 2 11.7 0.24 3.93 4.76 7.1X10-5 実施例 3 13.8 0.19 2.79 3.99 1. lXlO—4 実施例 4 13.3 0.16 4.34 4.95 6.5X10-5 比較例 8.7 0.44 2.87 4.00 Example 2 11.7 0.24 3.93 4.76 7.1X10-5 Example 3 13.8 0.19 2.79 3.99 1.lXlO- 4 Example 4 13.3 0.16 4.34 4.95 6.5X10-5 Comparative Example 8.7 0.44 2.87 4.00
[0029] これに対して、比較例 1の平均粒径は 8. 7 m、タップ密度が 4· 00gg/cm3であ る力 比表面積は 0.44m2/gと他の実施例と比較して高い数値であり、銀メツキ銅 微粉表面の凹凸が多ぐ銀メツキ表面の色調が悪ぐまた導電性も低下し、本願発明 の目的を達成することができず、好ましくない結果となった。 [0029] On the other hand, the average particle size of Comparative Example 1 is 8.7 m, the tap density is 4,000 gg / cm 3, and the force specific surface area is 0.44 m 2 / g, compared with the other examples. The silver-plated copper fine powder surface has many irregularities, the color tone of the silver-plated surface is poor, and the conductivity is lowered, so that the object of the present invention cannot be achieved, resulting in an undesirable result.
産業上の利用可能性 Industrial applicability
[0030] 本発明に係る銅微粉表面に銀層を均一に被覆した銀メツキ銅微粉は、優れた導電 [0030] The silver-plated copper fine powder in which the silver layer is uniformly coated on the surface of the copper fine powder according to the present invention has excellent conductivity.
X X X X
性を有するとともに銀メツキ反応時の再現性に優れ、原料銅微粉並みのタップ密度を 有するため、導電ペーストなどの電気的導通確保の材料に最適である。 In addition, it has excellent reproducibility during silver plating reaction and has a tap density similar to that of the raw material copper fine powder, making it ideal for materials that ensure electrical continuity such as conductive paste.
Claims
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011028985A (en) * | 2009-07-24 | 2011-02-10 | Fujikura Kasei Co Ltd | Method of manufacturing conductive paste, and the conductive paste |
| WO2011125556A1 (en) * | 2010-03-31 | 2011-10-13 | Jx日鉱日石金属株式会社 | Fine silver-plated copper powder and method for producing same |
| JP2012092376A (en) * | 2010-10-25 | 2012-05-17 | Ishihara Chem Co Ltd | Method of manufacturing tin plated copper powder |
| JP2012180563A (en) * | 2011-03-01 | 2012-09-20 | Mitsui Mining & Smelting Co Ltd | Copper particle |
| CN102773475A (en) * | 2012-07-31 | 2012-11-14 | 东南大学 | Copper oxide silver composite powder for conductive paste and preparation method thereof |
| CN103752842A (en) * | 2013-11-11 | 2014-04-30 | 南京工业大学 | Preparation of nano silver-coated copper powder by replacement and chemical deposition composite method |
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| CN117983808A (en) * | 2024-02-02 | 2024-05-07 | 有研纳微新材料(北京)有限公司 | Submicron silver-coated copper powder and preparation method thereof |
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| WO2015008628A1 (en) * | 2013-07-16 | 2015-01-22 | Dowaエレクトロニクス株式会社 | Silver-coated copper alloy powder and process for producing same |
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Also Published As
| Publication number | Publication date |
|---|---|
| TW200831214A (en) | 2008-08-01 |
| JPWO2008059789A1 (en) | 2010-03-04 |
| TWI349589B (en) | 2011-10-01 |
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