JPS60248803A - Production of silver powder - Google Patents

Production of silver powder

Info

Publication number
JPS60248803A
JPS60248803A JP10435884A JP10435884A JPS60248803A JP S60248803 A JPS60248803 A JP S60248803A JP 10435884 A JP10435884 A JP 10435884A JP 10435884 A JP10435884 A JP 10435884A JP S60248803 A JPS60248803 A JP S60248803A
Authority
JP
Japan
Prior art keywords
silver
silver powder
nitrate
soln
powder
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
JP10435884A
Other languages
Japanese (ja)
Other versions
JPH0319283B2 (en
Inventor
Hiroshi Morimoto
博 森本
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.)
Fukuda Kinzoku Hakufun Kogyo Kk
Fukuda Metal Foil and Powder Co Ltd
Original Assignee
Fukuda Kinzoku Hakufun Kogyo Kk
Fukuda Metal Foil and Powder 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 Fukuda Kinzoku Hakufun Kogyo Kk, Fukuda Metal Foil and Powder Co Ltd filed Critical Fukuda Kinzoku Hakufun Kogyo Kk
Priority to JP10435884A priority Critical patent/JPS60248803A/en
Publication of JPS60248803A publication Critical patent/JPS60248803A/en
Publication of JPH0319283B2 publication Critical patent/JPH0319283B2/ja
Granted legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

PURPOSE:To obtain silver powder for a conductive adhesive agent having a low concn. of residual ion and the narrow width of a grain size distribution in a method for adding a reducing agent to an aq. silver salt soln. and precipitating silver powder by using the specific aq. silver salt soln. CONSTITUTION:The reducing agent is added to the aq. ammonical silver nitrate soln. directly or after adding water soluble nitrate thereto to precipitate silver powder. The silver powder is thus obtd. The aq. ammonical silver nitrate soln. refers to the soln. prepd. by adding about >=30pts.wt. 30% ammonia water by 100pts.wt. silver nitrate to silver nitrate soln. The precipitated silver powder has the small width of the grain size distribution and has good reproducibility thereof even if the silver salt is reduced by hydrazine according to the above-mentioned method. Harmful residual ions are not contained in the precipitated silver powder if caustic alkali is not used and therefore a rinsing stage, etc. which are post-stage are made simpler.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、高純度で残留イオン濃度の少ない銀粉末の製
造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing silver powder with high purity and low residual ion concentration.

近年、IC−USI等の集積回路用の導電材として銀糸
導電性接着剤が多用されるようになっている。この接着
剤に用いられる銀粉末は、微細で粒度付布巾が小さく、
しかも集積回路に害を与えるイオン化しやすい物質、例
えばハロゲン元素やアルカリ金属等の残留イオン性物質
が5oppm以下の高純度の品質特性が要求される。 
本発明はこの集積回路用の導電性接着剤に使用する銀粉
末の製造方法に関するものである。
In recent years, silver thread conductive adhesives have come into widespread use as conductive materials for integrated circuits such as IC-USI. The silver powder used in this adhesive is fine and has a small particle size.
In addition, high purity quality characteristics are required, with residual ionic substances such as halogen elements and alkali metals being 5 oppm or less, which are easily ionized and harmful to integrated circuits.
The present invention relates to a method for producing silver powder used in a conductive adhesive for integrated circuits.

〔従来の技術〕[Conventional technology]

導電性接着剤に用いる銀粉末の一般的製造方法は、化学
還元置換析出法により製造される。この方法は銀塩水溶
液に還元剤を添加し銀粉末を析出させる方法であり、こ
こで用いられる還元剤は主として苛性アルカリである。
A common method for producing silver powder used in conductive adhesives is a chemical reduction substitution precipitation method. This method is a method in which a reducing agent is added to an aqueous silver salt solution to precipitate silver powder, and the reducing agent used here is mainly caustic alkali.

こうして得られる銀粉末は、苛性アルカリが残留イオン
として100ppm以」二根扮未に何着しているため、
集積回路に適用するのは好ましくない。又、還元剤とし
て苛性アルカリを使用しない場合、例えばヒドラジンで
還元した場合、析出する銀粉末の粒度分布中が大きくし
かも再現性のないものであった。
The silver powder obtained in this way contains more than 100 ppm of caustic alkali as residual ions, so
It is not desirable to apply it to integrated circuits. Further, when caustic alkali is not used as a reducing agent, for example when reduction is performed with hydrazine, the particle size distribution of the precipitated silver powder is large and is not reproducible.

〔本発明が解決しようとする問題点〕[Problems to be solved by the present invention]

本発明者は、前記の従来の技術の欠点を改良し、半導体
に有害となる残留イオン濃度が50ppm以下と少ない
銀粉末、及び粉末特性のバラツキが少ない品質の優れた
銀粉末の製造方法について鋭意研究した結果、本発明を
完成した。
The present inventors have made efforts to improve the drawbacks of the above-mentioned conventional techniques, and to develop a method for producing silver powder with a low residual ion concentration of 50 ppm or less, which is harmful to semiconductors, and a high-quality silver powder with less variation in powder properties. As a result of research, the present invention was completed.

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

本発明はアンモニア性硝酸銀水溶液に直接又は水溶性硝
酸塩を添加した後、還元剤を添加することにより銀粉を
析出させることを特徴とする銀粉末の製造方法である。
The present invention is a method for producing silver powder, characterized in that silver powder is precipitated by adding a reducing agent directly or after adding a water-soluble nitrate to an ammoniacal silver nitrate aqueous solution.

本発明に言うアンモニア性硝酸銀水溶液とは、硝酸銀1
00重量部に対して30%アンモニア水30重量部以上
(アンモニアとして9重量部以上、以下同じ)を硝酸銀
水溶液に添加したものである。
The ammoniacal silver nitrate aqueous solution referred to in the present invention refers to silver nitrate 1
00 parts by weight, 30 parts by weight or more of 30% ammonia water (9 parts by weight or more as ammonia, the same applies hereinafter) is added to an aqueous silver nitrate solution.

このアンモニア性硝酸銀水溶液を用いることにより従来
問題となっていたヒドラジンで還元した場合でも析出す
る銀粉末の粒度分布I11が小さく、しかも再現性の良
いものとなる。さらに、苛性アルカリを使用しない場合
は、析出した銀粉末に有害な残留イオンを含まないので
、後工程の水洗工程等が簡略化される。
By using this ammoniacal silver nitrate aqueous solution, even when reduced with hydrazine, which has been a problem in the past, the particle size distribution I11 of the precipitated silver powder is small and the reproducibility is good. Furthermore, when caustic alkali is not used, the precipitated silver powder does not contain harmful residual ions, so the post-process water washing step etc. is simplified.

本発明では水溶性硝酸塩を添加しなくても、高純度銀粉
末は得られるが、より粒度分布[11を狭く、また粒度
を調節するために水溶性硝酸塩を添加するほうがよい。
In the present invention, high purity silver powder can be obtained without adding water-soluble nitrate, but it is better to add water-soluble nitrate to narrow the particle size distribution [11] and to control the particle size.

ここで用いる水溶性硝酸塩は、硝酸銅又は硝酸亜鉛の1
種以上であり、添力d量は、アンモニア性硝酸銀水溶液
中の硝酸銀100重量部に対し0.5重量部〜10重量
部の範囲とするのが好ましい。その理由は、0.5重量
部以下では上記のような効果が少なく、10重量部以上
では、粒径調整の効果が飽和の状態になり、これ以上多
く添加しても効果の増大が得られないばかりでなく、逆
に残留不純物が増大し、高純度の銀粉末が得られなくな
るためである。
The water-soluble nitrate used here is copper nitrate or zinc nitrate.
The amount of additive d is preferably in the range of 0.5 parts by weight to 10 parts by weight based on 100 parts by weight of silver nitrate in the ammoniacal silver nitrate aqueous solution. The reason for this is that if it is less than 0.5 parts by weight, the above effect will be small, and if it is more than 10 parts by weight, the effect of particle size adjustment will be saturated, and even if more is added, the effect will not be increased. This is because not only is it not possible, but on the contrary, residual impurities increase, making it impossible to obtain highly pure silver powder.

本発明に用いる還元剤はホルマリン等のアルデヒドやヒ
ドラジンが使用できるが、ヒドラジンを用いる方が還元
効率の点で好ましい。
As the reducing agent used in the present invention, aldehydes such as formalin and hydrazine can be used, but it is preferable to use hydrazine in terms of reduction efficiency.

〔実施例〕〔Example〕

以下本発明の実施例について述べる。 Examples of the present invention will be described below.

実施例1゜ 硝酸銀水溶液(’AgNO3100g/HzO300m
l)に30%アンモニア水溶液30gを添加し、アンモ
ニア性硝酸銀水溶液とする。次ぎに抱水ヒドラジンを添
加し、白色の沈澱物を生成させる。この時アンモニア性
硝酸銀水溶液の根分が全て沈澱として生成芝るまで抱水
ヒドラジンを添加する。得られた沈澱物はデカンテーシ
ョンにより充分に水洗し、濾過した後低温乾燥を行った
。こうして得られた粉末は、平均粒径1.5μm、粒度
分布中が1μmで、水溶性のアルカリ物質及びハロゲン
物質を合わせた残留イオン濃度(以下単に残留イオン濃
度と言う)が20ppmの銀粉末であった。
Example 1゜Silver nitrate aqueous solution ('AgNO3100g/HzO300m
Add 30 g of a 30% ammonia aqueous solution to l) to obtain an ammoniacal silver nitrate aqueous solution. Hydrazine hydrate is then added to form a white precipitate. At this time, hydrazine hydrate is added until all the roots of the ammoniacal silver nitrate aqueous solution are formed as precipitates. The obtained precipitate was thoroughly washed with water by decantation, filtered, and then dried at low temperature. The powder thus obtained is a silver powder with an average particle size of 1.5 μm, a particle size distribution of 1 μm, and a residual ion concentration (hereinafter simply referred to as residual ion concentration) of 20 ppm including water-soluble alkaline substances and halogen substances. there were.

以上のようにして得られた銀粉末80重量部とエポキシ
樹脂接着剤20重量部を均一混練してペーストとしたも
のを150℃−30分間で硬化させると、比抵抗I X
 10−’Ω−cm、接着力50kg/cnjの特性を
もった導電性接着剤が得られた。
When a paste obtained by uniformly kneading 80 parts by weight of the silver powder obtained as described above and 20 parts by weight of the epoxy resin adhesive is cured at 150°C for 30 minutes, the specific resistance I
A conductive adhesive having characteristics of 10-'Ω-cm and adhesive strength of 50 kg/cnj was obtained.

実施例2゜ 硝酸銀水溶液(ΔgNto3100g/1Iz0300
 ml)に30%アンモニア水溶液40gを添加し、ア
ンモニア性硝酸銀水溶液とし硝酸銅(Cu(NO3) 
・611zOO,5g)を添加した。次ぎに抱水ヒドラ
ジンを添加し、白色の沈澱物を生成させた。こうして得
られた沈澱物を実施例1と同じ方法で濾過水洗を行った
。こうして得られた粉末は、平均粒径1.Opm、粒度
分布中1.5μmで、残留イオン濃度が30 p p 
m ′0)銀粉末であった。どの銀粉末をペースト化し
たものは実施例1と同等の特性をもっていた。
Example 2゜Silver nitrate aqueous solution (ΔgNto3100g/1Iz0300
ml) was added with 40 g of 30% ammonia aqueous solution to make an ammoniacal silver nitrate aqueous solution.
・611zOO, 5g) was added. Hydrazine hydrate was then added to form a white precipitate. The precipitate thus obtained was filtered and washed with water in the same manner as in Example 1. The powder thus obtained had an average particle size of 1. Opm, 1.5 μm in particle size distribution, residual ion concentration 30 p p
m'0) was silver powder. Which silver powder was made into a paste had the same characteristics as Example 1.

実施例3゜ 硝酸銀水溶液(八gNo3100g/Hz0300 m
l)に30%アンモニア水溶液40gを添加し、アンモ
ニア性硝酸銀水溶液とし硝酸亜鉛(Zn(NO+) z
・611z010g)を添加する。次ぎに抱水ヒドラジ
ンを添加し、灰黄色の沈澱物を生成させた。こうして得
られた沈澱物を実施例1と同じ方法で濾過水洗を行った
。こうして得られた粉末は、平均粒径0.2μm、粒度
分布巾が0.2μmで、残留イオン濃度が50ppmの
銀粉末であった。この銀粉末をペースト化したものは実
施例1と同等の特性をもっていた。
Example 3゜Silver nitrate aqueous solution (8gNo3100g/Hz0300m
40g of 30% ammonia aqueous solution was added to l) to make an ammoniacal silver nitrate aqueous solution and zinc nitrate (Zn(NO+) z
・Add 611z010g). Hydrazine hydrate was then added to form a gray-yellow precipitate. The precipitate thus obtained was filtered and washed with water in the same manner as in Example 1. The powder thus obtained was a silver powder with an average particle diameter of 0.2 μm, a particle size distribution width of 0.2 μm, and a residual ion concentration of 50 ppm. A paste obtained from this silver powder had properties equivalent to those of Example 1.

実施例4゜ 硝酸銀水溶液(八gN(h 100g/HzO300m
l)に30%アンモニア水溶液40g添加し、アンモニ
ア性硝酸銀水溶液とし硝酸銅・硝酸亜鉛を各々5g添加
した。
Example 4゜Silver nitrate aqueous solution (8 gN (h 100g/HzO300m
40 g of a 30% ammonia aqueous solution was added to l), and 5 g each of copper nitrate and zinc nitrate were added to make an ammoniacal silver nitrate aqueous solution.

次ぎに抱水ヒドラジンを添加し、灰色の沈澱物を化成さ
せた。こうして得られた沈澱物を実施例1と同じ方法で
濾過水洗を行った。こうして得られた粉末は平均粒径0
.08μm、粒度分布巾0.05μmで、残留イオン濃
度が50ppmの銀粉末であった。
Next, hydrazine hydrate was added to form a gray precipitate. The precipitate thus obtained was filtered and washed with water in the same manner as in Example 1. The powder thus obtained has an average particle size of 0
.. The silver powder had a particle size distribution width of 0.08 μm, a particle size distribution width of 0.05 μm, and a residual ion concentration of 50 ppm.

この銀粉末をペースト化したものの硬化物は、比抵抗5
x io−’Ω−cm、接着力50kg/cn+の特性
をもっていた。
The cured product made by turning this silver powder into a paste has a specific resistance of 5
x io-'Ω-cm and adhesive force of 50 kg/cn+.

比較例 硝酸銀水溶液(f1gN03100g/IIz0300
 ml)にポルマリン50m1を添加し次いで苛性ソー
ダ水溶液(NaO8100g/IILO200m1 )
を添加し、白色沈澱物を生成させる。こうして得られた
沈澱物を実施例1と同じ方法で濾過水洗を行った。こう
して得られた粉末は、粒径1.0μmで、残留イオン濃
度200ppmの銀粉末であった。
Comparative example Silver nitrate aqueous solution (f1gN03100g/IIz0300
ml), and then add a caustic soda aqueous solution (NaO8100g/IILO200ml).
is added to form a white precipitate. The precipitate thus obtained was filtered and washed with water in the same manner as in Example 1. The powder thus obtained was a silver powder with a particle size of 1.0 μm and a residual ion concentration of 200 ppm.

〔発明の効果〕〔Effect of the invention〕

本発明により得られた銀粉末は、残留イオンの少ない高
純度銀粉末であるため、半導体に使用される、導電性接
着剤の原料として好適である。
Since the silver powder obtained by the present invention is a high purity silver powder with few residual ions, it is suitable as a raw material for conductive adhesives used in semiconductors.

特許出願人 福田金属箔粉工業株式会社patent applicant Fukuda Metal Foil and Powder Industry Co., Ltd.

Claims (4)

【特許請求の範囲】[Claims] (1)アンモニア性硝酸銀水溶液に、直接又は水溶性硝
酸塩を添加した後、還元剤を添加することにより銀粉を
析出させることを特徴とする銀粉末の製造方法。
(1) A method for producing silver powder, which comprises adding a reducing agent directly or after adding a water-soluble nitrate to an ammoniacal silver nitrate aqueous solution to precipitate silver powder.
(2)水溶性硝酸塩が、硝酸銅又は硝酸亜鉛のうちいず
れか1種もしくは2種であることを特徴とする特許請求
範囲の第1項に記載の銀粉末の製造方法。
(2) The method for producing silver powder according to claim 1, wherein the water-soluble nitrate is one or both of copper nitrate and zinc nitrate.
(3)還元剤がヒ1゛ラシンであることを特徴とする特
許請求の範囲第1〜2項のいずれかに記載の銀粉末の製
造方法。
(3) The method for producing silver powder according to any one of claims 1 to 2, wherein the reducing agent is hyacin.
(4)水溶性硝酸塩の添加量がアンモニア性硝酸銀水溶
液中の硝酸銀100重量部に対し0.5〜10重量部で
あることを特徴とする特許請求の範囲第1項〜第3項の
いずれかに記載の銀粉末の製造方法。
(4) Any one of claims 1 to 3, characterized in that the amount of water-soluble nitrate added is 0.5 to 10 parts by weight per 100 parts by weight of silver nitrate in the ammoniacal silver nitrate aqueous solution. The method for producing silver powder described in .
JP10435884A 1984-05-22 1984-05-22 Production of silver powder Granted JPS60248803A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10435884A JPS60248803A (en) 1984-05-22 1984-05-22 Production of silver powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10435884A JPS60248803A (en) 1984-05-22 1984-05-22 Production of silver powder

Publications (2)

Publication Number Publication Date
JPS60248803A true JPS60248803A (en) 1985-12-09
JPH0319283B2 JPH0319283B2 (en) 1991-03-14

Family

ID=14378624

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10435884A Granted JPS60248803A (en) 1984-05-22 1984-05-22 Production of silver powder

Country Status (1)

Country Link
JP (1) JPS60248803A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62280308A (en) * 1986-05-30 1987-12-05 Mitsui Mining & Smelting Co Ltd Production of fine silver-palladium alloy power
JPS63115737A (en) * 1986-11-05 1988-05-20 松下電工株式会社 Electric laminated board
JP2008519156A (en) * 2004-10-29 2008-06-05 ナノダイナミクス,インク. Preparation of ultrafine metal powder in aqueous solution
JP2009235474A (en) * 2008-03-26 2009-10-15 Dowa Electronics Materials Co Ltd Method for producing silver powder
JPWO2020137330A1 (en) * 2018-12-26 2021-11-11 昭栄化学工業株式会社 Silver paste

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4842782A (en) * 1971-09-30 1973-06-21

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4842782A (en) * 1971-09-30 1973-06-21

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62280308A (en) * 1986-05-30 1987-12-05 Mitsui Mining & Smelting Co Ltd Production of fine silver-palladium alloy power
JPH0135044B2 (en) * 1986-05-30 1989-07-24 Mitsui Mining & Smelting Co
JPS63115737A (en) * 1986-11-05 1988-05-20 松下電工株式会社 Electric laminated board
JP2008519156A (en) * 2004-10-29 2008-06-05 ナノダイナミクス,インク. Preparation of ultrafine metal powder in aqueous solution
JP2009235474A (en) * 2008-03-26 2009-10-15 Dowa Electronics Materials Co Ltd Method for producing silver powder
JPWO2020137330A1 (en) * 2018-12-26 2021-11-11 昭栄化学工業株式会社 Silver paste
US12100530B2 (en) 2018-12-26 2024-09-24 Shoei Chemical Inc. Silver paste

Also Published As

Publication number Publication date
JPH0319283B2 (en) 1991-03-14

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