JPS63312906A - Production of fine silver alloy powder - Google Patents

Production of fine silver alloy powder

Info

Publication number
JPS63312906A
JPS63312906A JP14951687A JP14951687A JPS63312906A JP S63312906 A JPS63312906 A JP S63312906A JP 14951687 A JP14951687 A JP 14951687A JP 14951687 A JP14951687 A JP 14951687A JP S63312906 A JPS63312906 A JP S63312906A
Authority
JP
Japan
Prior art keywords
soln
acid
alloy powder
silver alloy
alloy
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.)
Granted
Application number
JP14951687A
Other languages
Japanese (ja)
Other versions
JP2550586B2 (en
Inventor
Takasumi Shimizu
孝純 清水
Tamotsu Nishinakagawa
西中川 保
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP62149516A priority Critical patent/JP2550586B2/en
Publication of JPS63312906A publication Critical patent/JPS63312906A/en
Application granted granted Critical
Publication of JP2550586B2 publication Critical patent/JP2550586B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To easily produce fine silver alloy powder having high purity at a low cost by mixing metals such as Pd with Ag, melting the mixture, dissolving the mixture with an acid to prepare a soln., adjusting the pH of the soln. with a basic soln., and adding a reducing agent to the soln. to reduce the metal ions. CONSTITUTION:The alloy base material is prepd. by mixing and melting 1 or >=2 kinds of the metals selected from Ag and a group consisting of Pd, In Au, Pt, and Sn. This alloy material is dissolved with the acid such as nitric acid to prepare the soln. of the metal salt of the acid. The pH of this soln. is adequately adjusted by adding the basic soln. such as aq. ammonia soln., thereto. The reducing agent such as hydrazine is then added to this soln. to reduce the metal ions and to co-precilitate the metals which are the components of the alloy base material. The alloy powder is thereby obtd. in the state of the fine powder without being grown or flocculated. The fine silver alloy powder having the high purity is thus produced.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は例えば厚膜ハイブリッドIC用導体ペーストに
用いられる銀合金微粉末の製造方法に関するものである
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing fine silver alloy powder used, for example, in a conductor paste for thick film hybrid ICs.

〔発明の背景〕[Background of the invention]

厚膜ハイブリッドIC等に用いられる導体ペーストには
Ag系の金属粉末が混合されている。しかしAg単独の
粉末であるとAg粉末のマイグレーションやハンダくわ
れ性等に問題があるのでAgとともにPdやptが併用
されている。しかしながら上記問題をより完全に解消す
るにはA。
Conductor paste used in thick film hybrid ICs and the like contains Ag-based metal powder mixed therein. However, if a powder of Ag alone is used, there are problems with migration of the Ag powder, solderability, etc., so Pd or pt is used in combination with Ag. However, to more completely solve the above problem, choose A.

粉末にPdやpt等の粉末を単に混合するよりもAgと
Pdやpt等を合金化して該合金を粉末化した方がより
一層望ましいことである。
It is much more desirable to alloy Ag with Pd, pt, etc. and turn the alloy into powder, rather than simply mixing powder with Pd, pt, etc.

〔従来の技術〕[Conventional technology]

従来、AK−Pd合金粉末を製造する方法としては、硝
酸銀−硝酸パラジウム混合溶液に炭酸ソ−ダを添加して
Ag−Pd複合炭酸塩として沈澱させ、該Ag−Pd複
合炭酸塩の沈澱物を水素により接触還元する方法、また
上記の炭酸ソーダに代えてカセイソーダを使用すること
により酸化銀と水酸化パラジウムとの混合沈澱物を生成
し、該混合沈澱物を水素中で80−180℃の温度範囲
で加熱して接触還元する方法(特願昭56−10882
1号)が提供されている。
Conventionally, as a method for producing AK-Pd alloy powder, sodium carbonate is added to a mixed solution of silver nitrate and palladium nitrate to precipitate an Ag-Pd composite carbonate, and the precipitate of the Ag-Pd composite carbonate is A mixed precipitate of silver oxide and palladium hydroxide is produced by a method of catalytic reduction with hydrogen, or by using caustic soda in place of the above-mentioned sodium carbonate, and the mixed precipitate is heated in hydrogen at a temperature of 80-180°C. Method of catalytic reduction by heating in a range (Patent application 1988-10882
No. 1) is provided.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら上記従来の方法では沈澱を水素中で加熱し
て接触還元させるために沈澱粒子が還元中に成長したり
凝集したりすることを防止することが出来ない。また組
成のコントロールを溶液の調整で行なうため目標組成の
ものを得ることも困難であり、条件により変化しやすい
、更に金属硝酸塩は金属単体(地金)に比して高価であ
る。金属地金を硝酸に溶解して金属硝酸塩を得れば金属
硝酸塩を購入するよりも安価になるが、Adの場合は硝
酸銀に簡単に溶解するけれどもptの場合は極めて溶解
しにくく、硝酸塩溶液を得るのが困難であると云う問題
点を有している。
However, in the above-mentioned conventional method, since the precipitate is heated in hydrogen for catalytic reduction, it is not possible to prevent the precipitate particles from growing or agglomerating during the reduction. Furthermore, since the composition is controlled by adjusting the solution, it is difficult to obtain a target composition, and it is easy to change depending on the conditions.Furthermore, metal nitrates are more expensive than simple metals (base metals). Obtaining metal nitrate by dissolving metal base metal in nitric acid will be cheaper than purchasing metal nitrate, but while Ad easily dissolves in silver nitrate, PT is extremely difficult to dissolve, so it is difficult to use a nitrate solution. The problem is that it is difficult to obtain.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は上記問題点を解除する手段として、Aにと、P
d 、In、Au、Pt、Snからなるグループから選
ばれた一種または二種以上の金属を混合溶解して合金母
材を製造する工程1 該合金母材を酸で溶解して溶液とする工程2該溶液に塩
基性溶液を添加することによってpHを調節した上で還
元剤を加えて該溶液中の金属イオンを還元する工程3 以上の工程1,2.3からなる銀合金微粉末の製造方法
を提供するものである。
The present invention provides A and P as means for solving the above problems.
Step 1 of producing an alloy base material by mixing and melting one or more metals selected from the group consisting of d, In, Au, Pt, and Sn. A step of dissolving the alloy base material with an acid to form a solution. 2 Step of adjusting the pH by adding a basic solution to the solution and adding a reducing agent to reduce metal ions in the solution 3 Production of silver alloy fine powder consisting of the above steps 1 and 2.3 The present invention provides a method.

本発明においては上気したようにまずAgと、Pd 、
In、Au、Pt、Snからなるグループから選ばれた
一種または二種以上の金属を混合し溶解して合金母材と
する(工程1)。
In the present invention, first, Ag, Pd,
One or more metals selected from the group consisting of In, Au, Pt, and Sn are mixed and melted to form an alloy base material (Step 1).

このようにして得られた該合金母材は酸で溶解せられて
核酸の金属塩の溶液となる(工程2)。
The alloy base material thus obtained is dissolved with acid to become a solution of the metal salt of nucleic acid (Step 2).

工程2において用いられる酸としては硫酸、塩酸、硝酸
等の無機酸、酢酸、蓚酸等の有機酸等その種類を問わな
いが、溶解が速やかなこと、導体ペーストに混入すると
有害なNa 、CI等のイオンを含まないこと等により
硝酸を使用することが望ましい。
The acids used in step 2 can be of any type, including inorganic acids such as sulfuric acid, hydrochloric acid, and nitric acid, and organic acids such as acetic acid and oxalic acid, but they must dissolve quickly and include Na, CI, etc., which are harmful if mixed into the conductor paste. It is desirable to use nitric acid because it does not contain ions.

工程2において生成された溶液は塩基性溶液を添加する
ことによってpHを調節した上で還元剤を加えて該溶液
中の金属イオンを還元する(工程3)。
The pH of the solution produced in step 2 is adjusted by adding a basic solution, and then a reducing agent is added to reduce the metal ions in the solution (step 3).

工程3において用いられる塩基性溶液はカセイソーダ、
カセイカリ、アンモニア等の無機塩基、ジエチルアミン
、トリエチルアミン、トリエタノールアミン、ピリジン
等の有機塩基等の水溶液、あるいはメタノール、エタノ
ール等の有機溶剤溶液であるが、 Na 、 CI−等
の導体ペーストに混入すると有害なイオンを含まない点
でアンモニアを使用することが望ましい。
The basic solution used in step 3 is caustic soda,
These are aqueous solutions of inorganic bases such as caustic potash and ammonia, organic bases such as diethylamine, triethylamine, triethanolamine, and pyridine, or solutions of organic solvents such as methanol and ethanol, but they are harmful when mixed with conductor pastes such as Na and CI-. It is desirable to use ammonia because it does not contain any harmful ions.

工程3において用いられる還元剤としては重亜硫酸ソー
ダ、次亜硫酸ソーダ、水素化ホウ素ナトリウム等の無機
還元剤、ヒドラジンおよびその化合物、アルコルビン酸
、ロンガリット、ホルムアルデヒド、ブドウ糖、アルコ
ール類等があるが。
Reducing agents used in step 3 include inorganic reducing agents such as sodium bisulfite, sodium hyposulfite, and sodium borohydride, hydrazine and its compounds, ascorbic acid, Rongalite, formaldehyde, glucose, and alcohols.

Na、B等の導体ペーストに混入すると有害なイオンを
含まずかつ還元力の強い点からみてヒドラジンおよびヒ
ドラジド、ビドラジニウム塩等のヒドラジン化合物を使
用することが望ましい。
It is desirable to use hydrazine and hydrazine compounds such as hydrazide and vidrazinium salts because they do not contain harmful ions such as Na and B when mixed into the conductor paste and have strong reducing power.

〔作用〕[Effect]

工程2において合金母材を酸で溶解すると該合金母材を
構成する夫夫の金属の核酸に関する塩が生成されて該塩
の混合水溶液が得られる。即ち母合金の組成に一致した
混合水溶液となる。該合金母材中に単独では酸に溶解し
にくいPd、 I n、 Au。
In step 2, when the alloy base material is dissolved with an acid, a salt related to the nucleic acid of the husband metal constituting the alloy base material is generated, and a mixed aqueous solution of the salt is obtained. That is, a mixed aqueous solution matching the composition of the master alloy is obtained. Pd, In, and Au, which alone are difficult to dissolve in acid, are contained in the alloy base material.

ptが含まれていても、該合金中にあってはこれら難溶
性金属も速やかに酸に溶解する。
Even if pt is contained in the alloy, these poorly soluble metals are quickly dissolved in acid.

工程3において塩基性溶液を添加すると工程1において
生成した金属塩は金属水酸化物もしくは錯塩に変化する
。そして該pH値はまた得られる銀合金粉末の粒径を支
配する。pH値と粒径との関係を例示すればpH3〜5
で0.1μm以下、pH5〜7で0.1〜0.5μs、
pH7〜10で0.5〜1 pm、 pH10〜12で
1〜5μmである。
When a basic solution is added in step 3, the metal salt produced in step 1 changes into metal hydroxide or complex salt. And the pH value also governs the particle size of the resulting silver alloy powder. An example of the relationship between pH value and particle size is pH 3 to 5.
0.1 μm or less at pH 5-7, 0.1-0.5 μs at pH 5-7,
It is 0.5-1 pm at pH 7-10, and 1-5 μm at pH 10-12.

上記のようにして工程2において得られた溶液のpHを
塩基性溶液によって調節した上で還元剤を添加すると該
溶液に含まれている金属イオンは還元され合金母材の成
分である金属が共沈して合金粉末が得られる。該合金粉
末は採集され加熱等が及ぼされることがないので成長し
たり凝集したりすることがなく微粉末の状態のままで得
られる。
When the pH of the solution obtained in step 2 as described above is adjusted with a basic solution and a reducing agent is added, the metal ions contained in the solution are reduced and the metals that are the components of the alloy base material are Alloy powder is obtained by precipitation. Since the alloy powder is collected and is not subjected to heating or the like, it does not grow or agglomerate and can be obtained in a fine powder state.

〔発明の効果〕〔Effect of the invention〕

したがって本発明においては高純度の銀合金微粉末が安
価にかつ容易に得られる。
Therefore, in the present invention, high purity silver alloy fine powder can be obtained easily and inexpensively.

Claims (4)

【特許請求の範囲】[Claims] (1)Agと、Pd、In、Au、Pt、Snからなる
グループから選ばれた一種または二種以上の金属を混合
溶解して合金母材を製造する工程1該合金母材を酸で溶
解して溶液とする工程2該溶液に塩基性溶液を添加する
ことによってpHを調節した上で還元剤を加えて該溶液
中の金属イオンを還元する工程3 以上の工程1、2、3からなる銀合金微粉末の製造方法
(1) Process of producing an alloy base material by mixing and melting Ag and one or more metals selected from the group consisting of Pd, In, Au, Pt, and Sn 1 Melting the alloy base material with acid Step 2: Adjusting the pH by adding a basic solution to the solution, and then adding a reducing agent to reduce the metal ions in the solution. Step 3: Consisting of the above steps 1, 2, and 3. Manufacturing method of silver alloy fine powder
(2)工程2で用いる酸は硝酸である「特許請求の範囲
第(1)項」に記載の銀合金微粉末の製造方法
(2) The method for producing fine silver alloy powder according to "Claim (1)", wherein the acid used in step 2 is nitric acid.
(3)工程3で用いる塩基性溶液はアンモニア水溶液で
ある「特許請求の範囲第(1)項」に記載の銀合金微粉
末の製造方法
(3) The method for producing a fine silver alloy powder according to claim (1), wherein the basic solution used in step 3 is an ammonia aqueous solution.
(4)工程3で用いる還元剤がヒドラジンおよびその化
合物である「特許請求の範囲第(1)項」に記載の銀合
金微粉末の製造方法
(4) The method for producing a fine silver alloy powder according to claim (1), wherein the reducing agent used in step 3 is hydrazine and its compound.
JP62149516A 1987-06-16 1987-06-16 Method for producing fine silver alloy powder Expired - Lifetime JP2550586B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62149516A JP2550586B2 (en) 1987-06-16 1987-06-16 Method for producing fine silver alloy powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62149516A JP2550586B2 (en) 1987-06-16 1987-06-16 Method for producing fine silver alloy powder

Publications (2)

Publication Number Publication Date
JPS63312906A true JPS63312906A (en) 1988-12-21
JP2550586B2 JP2550586B2 (en) 1996-11-06

Family

ID=15476846

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62149516A Expired - Lifetime JP2550586B2 (en) 1987-06-16 1987-06-16 Method for producing fine silver alloy powder

Country Status (1)

Country Link
JP (1) JP2550586B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02294416A (en) * 1989-05-09 1990-12-05 Ishifuku Kinzoku Kogyo Kk Production of platinum powder
JPH03126805A (en) * 1989-10-12 1991-05-30 Kojundo Chem Lab Co Ltd Manufacture of ag-pd alloy powder for thick film paste
JPH0459904A (en) * 1990-06-28 1992-02-26 Sumitomo Metal Mining Co Ltd Manufacture of silver fine powder
KR100449369B1 (en) * 2001-11-29 2004-09-18 한국지질자원연구원 Preparation of flake-type fine silver powders
JP2007533862A (en) * 2004-04-22 2007-11-22 本田技研工業株式会社 Metal and alloy nanoparticles and methods for their synthesis
WO2012124046A1 (en) * 2011-03-14 2012-09-20 エム・テクニック株式会社 Manufacturing method for metal microparticles

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02294416A (en) * 1989-05-09 1990-12-05 Ishifuku Kinzoku Kogyo Kk Production of platinum powder
JPH03126805A (en) * 1989-10-12 1991-05-30 Kojundo Chem Lab Co Ltd Manufacture of ag-pd alloy powder for thick film paste
JPH0459904A (en) * 1990-06-28 1992-02-26 Sumitomo Metal Mining Co Ltd Manufacture of silver fine powder
KR100449369B1 (en) * 2001-11-29 2004-09-18 한국지질자원연구원 Preparation of flake-type fine silver powders
JP2007533862A (en) * 2004-04-22 2007-11-22 本田技研工業株式会社 Metal and alloy nanoparticles and methods for their synthesis
WO2012124046A1 (en) * 2011-03-14 2012-09-20 エム・テクニック株式会社 Manufacturing method for metal microparticles
CN103282145A (en) * 2011-03-14 2013-09-04 M技术株式会社 Manufacturing method for metal microparticles
US9387536B2 (en) 2011-03-14 2016-07-12 M. Technique Co., Ltd. Method for producing metal microparticles

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