JPH04323310A - Manufacturing method of metal fine powder - Google Patents

Manufacturing method of metal fine powder

Info

Publication number
JPH04323310A
JPH04323310A JP10888591A JP10888591A JPH04323310A JP H04323310 A JPH04323310 A JP H04323310A JP 10888591 A JP10888591 A JP 10888591A JP 10888591 A JP10888591 A JP 10888591A JP H04323310 A JPH04323310 A JP H04323310A
Authority
JP
Japan
Prior art keywords
metal
soln
fine metal
powder
fine
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.)
Pending
Application number
JP10888591A
Other languages
Japanese (ja)
Inventor
Osamu Kato
理 加藤
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 JP10888591A priority Critical patent/JPH04323310A/en
Publication of JPH04323310A publication Critical patent/JPH04323310A/en
Pending legal-status Critical Current

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  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)

Abstract

PURPOSE:To easily produce a fine metal powder having a specified grain shape by forming the complex of the metal dissolved in an aq. solvent contg. acid with a base, adjusting the soln. to specified pH and then adding a reducing agent at a specified temp. CONSTITUTION:One or more kinds of metal, alloy and metallic salt as the raw material are dissolved in an aq. solvent contg. acid such as hydrochloric acid and acetic acid. The metal concn. in the soln. is controlled to about 0.05-100g/l in accordance with the grain diameter of the depositing fine metal powder. A base such as ammonia forming the complex of the metal in the raw material is then added to the soln. to adjust the soln. to about pH8-11. The grain size distribution can be adjusted by the pH value. The soln. is kept at a specified temp. corresponding to the desired shape of the fine metal powder to be obtained, and a reducing agent such as hydrazine is added to deposit the fine metal powder. In this case, a globular fine metal grain is obtained at the soln. temp. of 10-30 deg.C, and a polyhedral fine metal powder is obtained at the soln. temp. of >=50 deg.C.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、所定の粒子形状を有す
る金属微粉末の製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing fine metal powder having a predetermined particle shape.

【0002】0002

【従来の技術】エレクトロニクス回路印刷の導電性ペー
スト、電磁波シールド塗料、電磁波シールド成形物射出
成形用のプラスチックペレット等には金属微粉末が混合
されている。このような分野で使用される金属微粉末に
あっては印刷適性、塗装適性、成形性等の面からみて粒
形が球状の金属微粉末の使用が望ましい。しかし導電性
、電磁波シールド性の面からみると、金属微粉末の粒子
相互の接触を密ならしめるためには粒形が多面体状であ
ることが望ましい。したがって粒形が球状の金属微粉末
と粒形が多面体状の金属微粉末とが混合して使用される
ことが多い。また金属微粉末からなる成形体を焼結して
焼結成形体を得る粉末冶金の分野でも、焼結温度や焼成
温度の調節、焼結成形体の充填密度や表面平滑性の調整
のために、種々な粒形の金属微粉末が要求されている。
2. Description of the Related Art Fine metal powder is mixed into conductive pastes for printing electronic circuits, electromagnetic shielding paints, plastic pellets for injection molding of electromagnetic shielding moldings, and the like. Regarding fine metal powders used in such fields, it is desirable to use fine metal powders with spherical particle shapes in view of printing suitability, coating suitability, moldability, etc. However, from the viewpoint of conductivity and electromagnetic shielding properties, it is desirable that the grains have a polyhedral shape in order to achieve close contact between the particles of the metal fine powder. Therefore, fine metal powder with spherical grain shape and fine metal powder with polyhedral grain shape are often used as a mixture. In addition, in the field of powder metallurgy, in which a sintered compact is obtained by sintering a compact made of fine metal powder, various methods are used to adjust the sintering temperature, the firing temperature, and the packing density and surface smoothness of the sintered compact. There is a demand for fine metal powder with a specific particle shape.

【0003】従来から、この種の金属微粉末の製造方法
にあっては、金属または金属塩を酸性水性溶媒中に溶解
し、塩基で中和した上で還元剤で還元して金属微粉末を
析出させる湿式法が提供されている。
Conventionally, in the production method of this type of metal fine powder, metal or metal salt is dissolved in an acidic aqueous solvent, neutralized with a base, and then reduced with a reducing agent to obtain metal fine powder. Wet methods of precipitation are provided.

【0004】0004

【発明が解決しようとする課題】しかしながら、上記従
来の湿式法にあっては、粒形を任意に調整することが困
難であるとされていた。
[Problems to be Solved by the Invention] However, in the conventional wet method described above, it is difficult to arbitrarily adjust the particle shape.

【0005】[0005]

【課題を解決するための手段】本発明は上記従来の課題
を解決するための手段として、金属、合金および金属塩
からなる組から選ばれた一種または二種以上の原料を酸
を含む水性溶媒中に溶解する工程1 該溶液に上記金属または合金を構成する金属の錯体を形
成する塩基を添加して所定のpH値に調節する工程2p
H調節後、得られる金属微粉末の目的形状に応じて所定
温度に維持しつゝ還元剤を添加して、金属微粉末を析出
させる工程3 以上の工程1,2,3からなる金属微粉末の製造方法を
提供するものである。本発明を以下に詳細に説明する。
[Means for Solving the Problems] As a means for solving the above-mentioned conventional problems, the present invention provides one or more raw materials selected from the group consisting of metals, alloys, and metal salts in an aqueous solvent containing an acid. Step 1 of dissolving in the solution Step 2 of adjusting the pH value to a predetermined value by adding a base that forms a complex of the metal or metal constituting the alloy to the solution
After H adjustment, a reducing agent is added to precipitate the metal fine powder while maintaining the temperature at a predetermined temperature depending on the desired shape of the metal fine powder obtained. Step 3. The metal fine powder consists of the above steps 1, 2, and 3. The present invention provides a method for manufacturing. The invention will be explained in detail below.

【0006】本発明に用いられる原料としての金属また
は合金を構成する金属としては、例えばAg,Pd,C
d,Co,Fe,Ni,Sn,Pb,Pt,Au,Cu
 等従来から導電性ペースト、電磁波シールド塗料、電
磁波シールド成形物、粉末冶金等の分野に使用されてい
た金属や合金あるいは化合物のすべてを包含する。また
本発明に用いられる原料としての金属塩としては、例え
ば上記例示した金属または合金あるいは化合物を構成す
る金属の塩酸塩、硫酸塩、硝酸塩、炭酸塩、酢酸塩等の
無機酸あるいは有機酸の塩のすべてが包含される。本発
明においては、上記金属および/または上記合金と上記
金属塩とは併用されてもよく、また二種以上が混合され
てもよい。
[0006] Examples of metals constituting raw materials or alloys used in the present invention include Ag, Pd, and C.
d, Co, Fe, Ni, Sn, Pb, Pt, Au, Cu
It includes all metals, alloys, and compounds conventionally used in fields such as conductive pastes, electromagnetic shielding paints, electromagnetic shielding moldings, and powder metallurgy. Metal salts as raw materials used in the present invention include, for example, salts of inorganic or organic acids such as hydrochlorides, sulfates, nitrates, carbonates, and acetates of metals constituting the metals, alloys, or compounds listed above. All are included. In the present invention, the above-mentioned metal and/or the above-mentioned alloy and the above-mentioned metal salt may be used in combination, or two or more types may be mixed.

【0007】工程1においては、上記金属、合金および
金属塩からなる組から選ばれた一種または二種以上の原
料を酸を含む水性溶媒中に溶解する。上記酸を含む水性
溶媒とは塩酸、硫酸、酢酸等の無機酸あるいは有機酸を
含む水性溶媒であり、該水性溶媒としては水単独、ある
いは水に例えばメタノール、エタノール、イソプロパノ
ール、エチレングリコール、プロピレングリコール、ア
セトン、テトラヒドロフラン等の水混和性有機溶媒を所
定量混合した混合溶媒を用いる。
In step 1, one or more raw materials selected from the group consisting of the metals, alloys and metal salts mentioned above are dissolved in an aqueous solvent containing an acid. The above-mentioned acid-containing aqueous solvent is an aqueous solvent containing an inorganic or organic acid such as hydrochloric acid, sulfuric acid, acetic acid, etc. The aqueous solvent may be water alone, or water combined with methanol, ethanol, isopropanol, ethylene glycol, propylene glycol, etc. A mixed solvent prepared by mixing a predetermined amount of water-miscible organic solvents such as , acetone, and tetrahydrofuran is used.

【0008】上記工程1において溶液中の金属濃度は例
えば0.05〜100g/lと広い範囲が適用されるが
、金属濃度によって析出する金属微粉末の粒径を調節す
ることが出来る。即ち該溶液の金属濃度が高くなれば得
られる金属微粉末の粒径は大きくなる。また工程1を能
率良く行なうためには金属、合金および金属塩からなる
組から選ばれた一種または二種以上の原料を最初に濃厚
な酸溶液に溶解し、ついで所定の濃度に希釈することが
望ましい。濃厚溶液を用いれば、上記原料は速やかに溶
解する。
[0008] In the above step 1, the metal concentration in the solution is applied in a wide range, for example, from 0.05 to 100 g/l, and the particle size of the precipitated metal fine powder can be adjusted depending on the metal concentration. That is, as the metal concentration of the solution increases, the particle size of the obtained metal fine powder increases. In addition, in order to perform step 1 efficiently, it is necessary to first dissolve one or more raw materials selected from the group consisting of metals, alloys, and metal salts in a concentrated acid solution, and then dilute it to a predetermined concentration. desirable. If a concentrated solution is used, the above raw materials will dissolve quickly.

【0009】工程2においては、上記溶液に上記金属ま
たは合金を構成する金属の錯体を形成する塩基を添加し
て所定のpH値に調節する。該塩基としては、アンモニ
アあるいはジメチルアミン、トリエチルアミン、ジイソ
プロピルアミン、トリエタノールアミン、ジイソプロパ
ノールアミン等のアミン類が例示される。
In step 2, a base that forms a complex of the metal or metal constituting the alloy is added to the solution to adjust the pH to a predetermined value. Examples of the base include ammonia or amines such as dimethylamine, triethylamine, diisopropylamine, triethanolamine, and diisopropanolamine.

【0010】上記工程2において望ましいpH値範囲は
8〜11、更に望ましくは9〜11である。本発明では
上記pH値範囲において、pH値が低いと粒度分布が広
くなり、pH値が高いと粒度分布が狭くなることが解明
された。したがってpH値を調節することにより粒度分
布の広がりが調節可能となる。したがって粒度均一な金
属微粉末を得んとする場合には、工程2におけるpH値
を高くすればよい。しかしながらpH値が11以上にな
ると金属微粉末の形状が球状のもののみならずフレーク
状等の異形のものが生じるので、pH値は11以下に止
めることが望ましい。
[0010] In the above step 2, the desirable pH value range is 8-11, more preferably 9-11. In the present invention, it has been found that in the above pH value range, when the pH value is low, the particle size distribution becomes wide, and when the pH value is high, the particle size distribution becomes narrow. Therefore, by adjusting the pH value, the breadth of the particle size distribution can be adjusted. Therefore, if it is desired to obtain fine metal powder with uniform particle size, the pH value in step 2 may be increased. However, if the pH value is 11 or more, the shape of the metal fine powder will not only be spherical but also irregularly shaped such as flakes, so it is desirable to keep the pH value at 11 or less.

【0011】工程3においては、上記所定のpH値に調
節された溶液に還元剤を添加する。この際用いられる還
元剤としてはヒドラジン、アスコルビン酸、ブドウ糖等
の有機還元剤やチオ硫酸ソーダ、次亜硫酸ソーダ等の無
機還元剤があるが、望ましくは金属元素を含まないヒド
ラジンのような還元剤が使用される。
[0011] In step 3, a reducing agent is added to the solution adjusted to a predetermined pH value. Reducing agents used at this time include organic reducing agents such as hydrazine, ascorbic acid, and glucose, and inorganic reducing agents such as sodium thiosulfate and sodium hyposulfite, but desirably, a reducing agent such as hydrazine that does not contain metal elements is used. used.

【0012】上記還元工程では発熱をみるが、本発明で
は還元工程の温度により金属微粉末の粒子形状を調整し
得ることが解明された。即ち温度が50℃以上では多面
体状の粒形を有する金属微粒子が得られ、温度が30℃
以下では球状の粒形を有する金属微粒子が得られる。ま
た40℃付近では球状粒子と多面体粒子とが混合した金
属微粉末が得られる。しかし10℃以下になると還元反
応が円滑に進まなくなる。したがって上記還元工程は1
0℃以上で行なうことが望ましい。工程3において、溶
液中から金属が還元されて析出する。この場合の金属は
工程2におけるpH値により所定の粒度分布を有する微
粉末として得られる。得られた金属微粉末は濾別、遠心
分離等により溶媒から分離し、水洗、またメタノール、
エタノール、イソプロパノール等の水混和性溶媒で洗滌
した後乾燥する。
[0012] Although heat is generated in the above-mentioned reduction step, it has been found in the present invention that the particle shape of the fine metal powder can be adjusted by adjusting the temperature of the reduction step. That is, when the temperature is 50°C or higher, metal fine particles having a polyhedral shape are obtained, and when the temperature is 30°C
In the following, metal fine particles having a spherical particle shape are obtained. Further, at around 40° C., a fine metal powder containing a mixture of spherical particles and polyhedral particles is obtained. However, if the temperature drops below 10°C, the reduction reaction will not proceed smoothly. Therefore, the above reduction step is 1
It is desirable to carry out the process at a temperature of 0°C or higher. In step 3, the metal is reduced and precipitated from the solution. In this case, the metal is obtained as a fine powder having a predetermined particle size distribution depending on the pH value in step 2. The obtained metal fine powder is separated from the solvent by filtration, centrifugation, etc., washed with water, and mixed with methanol,
Wash with a water-miscible solvent such as ethanol or isopropanol, and then dry.

【0013】[0013]

【作用】工程3において、溶液中から金属が還元されて
粒子として析出するメカニズムとしては、LaMerモ
デルが提供されている。即ち、工程3の還元反応におい
て金属塩が還元されて金属になると、金属は溶液中に析
出して来る。そしてLaMerモデルによれば、まず粒
子の核が析出し、次いで該核のまわりの懸濁原子が該核
表面に付着して、該核表面の安定化位置に向かって移動
し、該安定化位置で核表面と結合して粒子成長が行なわ
れる。ところが低温では原子の易動度が小さくなり、核
表面の安定化位置まで原子がたどりつく前に核表面に捕
捉され結合してしまう。
[Operation] In step 3, the LaMer model is provided as the mechanism by which the metal is reduced from the solution and precipitated as particles. That is, when the metal salt is reduced to a metal in the reduction reaction in step 3, the metal is precipitated into the solution. According to the LaMer model, the nucleus of the particle precipitates first, and then the suspended atoms around the nucleus attach to the surface of the nucleus and move toward the stabilization position on the surface of the nucleus. At this point, the particles combine with the nuclear surface and particle growth occurs. However, at low temperatures, the mobility of atoms decreases, and atoms are captured and bonded to the nuclear surface before they reach a stable position on the nuclear surface.

【0014】即ち高温(例えば50℃以上)では原子は
核表面の安定化位置にたどりつくに充分な易動度を有し
、その結果粒子は多面体結晶形となり、低温(例えば3
0℃以下)では原子は核表面の安定化位置までたどりつ
くことが出来なくなってランダムな非結晶形、即ち球状
の粒子が析出されるのである。
That is, at high temperatures (eg, 50° C. or higher), the atoms have sufficient mobility to reach stable positions on the nuclear surface, so that the particles have a polyhedral crystal shape, and at low temperatures (eg, 3
(below 0°C), atoms cannot reach the stabilizing position on the nuclear surface, and random amorphous particles, ie, spherical particles, are precipitated.

【0015】[0015]

【実施例】【Example】

〔実施例1〕Ag :Pd =7:3重量比になるよう
にAg −Pd 合金を作製し、該合金を(2+1)硝
酸によって溶解する。この時の溶液の合金濃度はAg 
+Pd として400g/lになるように調整する。そ
の後水で該濃厚溶液を希釈してAg +Pdとして10
0g/lとなるように調節する(工程1)。上記溶液に
20重量%アンモニア水を添加してpH9に調節する(
工程2)。pHを調節した後は液温を所定温度に維持し
てヒドラジンをAg +Pd 100gあたり43cc
添加して還元を行なう(工程3)。この際のヒドラジン
の添加速度は1cc/分とする。かくしてAg :Pd
 =7:3重量比のAg −Pd 共沈金属微粉末を得
る。該Ag −Pd 微粉末は濾別後水洗し、次いでイ
ソプロパノールにて洗滌した後窒素気流中で乾燥する。 得られたAg −Pd 微粉末の粒度分布と工程3にお
ける還元温度との関係を図1に示す。図1によれば液温
が低くなるにつれて粒度分布が狭くなることが分かる。
[Example 1] An Ag--Pd alloy was prepared so that the weight ratio of Ag:Pd was 7:3, and the alloy was dissolved with (2+1) nitric acid. The alloy concentration of the solution at this time is Ag
+Pd is adjusted to 400g/l. The concentrated solution was then diluted with water to give 10% Ag + Pd.
Adjust to 0 g/l (Step 1). Add 20% by weight aqueous ammonia to the above solution to adjust the pH to 9 (
Step 2). After adjusting the pH, maintain the liquid temperature at a predetermined temperature and add 43cc of hydrazine per 100g of Ag + Pd.
is added to perform reduction (Step 3). The addition rate of hydrazine at this time is 1 cc/min. Thus Ag:Pd
Ag-Pd co-precipitated metal fine powder with a weight ratio of =7:3 is obtained. The Ag-Pd fine powder is filtered and washed with water, then with isopropanol, and then dried in a nitrogen stream. The relationship between the particle size distribution of the obtained Ag-Pd fine powder and the reduction temperature in step 3 is shown in FIG. According to FIG. 1, it can be seen that the particle size distribution becomes narrower as the liquid temperature becomes lower.

【0016】更に得られたAg −Pd 微粉末の粒子
形状と工程3における還元温度との関係を表1に示す。
Furthermore, Table 1 shows the relationship between the particle shape of the obtained Ag--Pd fine powder and the reduction temperature in step 3.

【表1】   表1によれば還元温度が30℃以下では球状粒形の
微粉末が得られ、40℃では球状粒形−多面体状粒形の
混合微粉末が得られ、50℃以上になると多面体状粒形
の微粉末が得られることが分かる。
[Table 1] According to Table 1, when the reduction temperature is 30°C or lower, a fine powder with a spherical grain shape is obtained, at 40°C a mixed fine powder with a spherical grain shape and a polyhedral grain shape is obtained, and at a reduction temperature of 50°C or higher, a mixed fine powder with a spherical grain shape and a polyhedral grain shape is obtained. It can be seen that a fine powder having a polyhedral grain shape is obtained.

【0017】このように本発明では工程3の還元温度を
調節することにより所望の粒子形状の金属微粉末を簡単
に得ることが出来る。
As described above, according to the present invention, by adjusting the reduction temperature in step 3, it is possible to easily obtain fine metal powder having a desired particle shape.

【0018】なお本実施例は本発明を限定するものでは
なく、金属微粉末の洗滌はメタノール、エタノール等の
イソプロパノール以外の水混和性溶媒が単独または混合
して使用されてもよく、また洗滌後の金属微粉末の乾燥
は窒素気流中でなくてもよく、減圧下で乾燥してもよい
Note that this example does not limit the present invention, and water-miscible solvents other than isopropanol, such as methanol and ethanol, may be used alone or in combination for washing the fine metal powder. The fine metal powder may not be dried in a nitrogen stream, but may be dried under reduced pressure.

【0019】[0019]

【発明の効果】したがって本発明では簡単な手段で所望
の形状の粒子を得ることが出来る。
[Effects of the Invention] Therefore, according to the present invention, particles having a desired shape can be obtained by simple means.

【0020】[0020]

【図面の簡単な説明】[Brief explanation of drawings]

【図1】工程3における還元温度と得られた金属微粉末
の粒度分布との関係を示すグラフである。
FIG. 1 is a graph showing the relationship between the reduction temperature in Step 3 and the particle size distribution of the obtained fine metal powder.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】金属、合金および金属塩からなる組から選
ばれた一種または二種以上の原料を酸を含む水性溶媒中
に溶解する工程1 該溶液に上記金属または合金を構成する金属の錯体を形
成する塩基を添加して所定のpH値に調節する工程2p
H調節後、得られる金属微粉末の目的形状に応じて所定
温度に維持しつゝ還元剤を添加して、金属微粉末を析出
させる工程3 以上の工程1,2,3からなることを特徴とする金属微
粉末の製造方法
Claim 1: Step 1 of dissolving one or more raw materials selected from the group consisting of metals, alloys, and metal salts in an acid-containing aqueous solvent; A complex of the metals constituting the metal or alloy is added to the solution. Step 2 of adjusting the pH value to a predetermined value by adding a base that forms
After H adjustment, a reducing agent is added to precipitate the metal fine powder while maintaining it at a predetermined temperature depending on the desired shape of the obtained metal fine powder.Step 3: It is characterized by comprising the above steps 1, 2, and 3. Method for producing fine metal powder
【請求項2】工程3において、球状の金属微粒子を得る
ことを目的として、温度を10〜30℃に調節すること
を特徴とする金属微粉末の製造方法
2. A method for producing fine metal powder, characterized in that in step 3, the temperature is adjusted to 10 to 30°C for the purpose of obtaining spherical fine metal particles.
【請求項3】工程3において、多面体状の金属微粒子を
得ることを目的として、温度を50℃以上に調節するこ
とを特徴とする金属微粉末の製造方法
3. A method for producing fine metal powder, characterized in that in step 3, the temperature is adjusted to 50° C. or higher for the purpose of obtaining polyhedral fine metal particles.
JP10888591A 1991-04-12 1991-04-12 Manufacturing method of metal fine powder Pending JPH04323310A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10888591A JPH04323310A (en) 1991-04-12 1991-04-12 Manufacturing method of metal fine powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10888591A JPH04323310A (en) 1991-04-12 1991-04-12 Manufacturing method of metal fine powder

Publications (1)

Publication Number Publication Date
JPH04323310A true JPH04323310A (en) 1992-11-12

Family

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Country Link
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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5389122A (en) * 1993-07-13 1995-02-14 E. I. Du Pont De Nemours And Company Process for making finely divided, dense packing, spherical shaped silver particles
WO2002081131A1 (en) * 2001-03-30 2002-10-17 Catalysts & Chemicals Industries Co., Ltd. Fine metal particles, method for preparing said particles, coating liquid containing said fine particles for forming transparent electroconductive film, substrate with transparent electroconductive film, and display
JP2003049202A (en) * 2001-08-09 2003-02-21 Dowa Mining Co Ltd Silver particles, method for producing the same and conductor paste
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JP2005298891A (en) * 2004-04-09 2005-10-27 Mitsubishi Materials Corp Method for producing metal fine particles and composition containing the same
WO2007008218A3 (en) * 2004-08-02 2007-03-15 Univ Florida High aspect ratio metal particles and methods for forming same
JP2008001974A (en) * 2006-03-31 2008-01-10 Dowa Holdings Co Ltd Silver powder and method for producing the same
US8182574B2 (en) 2003-09-05 2012-05-22 Mitsubishi Materials Corporation Metal fine particles, composition containing the same, and production method for producing metal fine particles
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Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5389122A (en) * 1993-07-13 1995-02-14 E. I. Du Pont De Nemours And Company Process for making finely divided, dense packing, spherical shaped silver particles
US7494710B2 (en) 2001-03-30 2009-02-24 Jgc Catalysts And Chemicals Ltd. Fine metal particles suitable for forming a conductive coating film
WO2002081131A1 (en) * 2001-03-30 2002-10-17 Catalysts & Chemicals Industries Co., Ltd. Fine metal particles, method for preparing said particles, coating liquid containing said fine particles for forming transparent electroconductive film, substrate with transparent electroconductive film, and display
JP2003049202A (en) * 2001-08-09 2003-02-21 Dowa Mining Co Ltd Silver particles, method for producing the same and conductor paste
EP2165791A3 (en) * 2003-09-05 2010-04-14 Mitsubishi Materials Corporation Metal microparticle, composition containing the same and process for producing metal microparticle
EP2165791A2 (en) 2003-09-05 2010-03-24 Mitsubishi Materials Corporation Metal microparticle, composition containing the same and process for producing metal microparticle
WO2005023466A1 (en) * 2003-09-05 2005-03-17 Mitsubishi Materials Corporation Metal microparticle, composition containing the same and process for producing metal microparticle
US8182574B2 (en) 2003-09-05 2012-05-22 Mitsubishi Materials Corporation Metal fine particles, composition containing the same, and production method for producing metal fine particles
JP2005298891A (en) * 2004-04-09 2005-10-27 Mitsubishi Materials Corp Method for producing metal fine particles and composition containing the same
WO2007008218A3 (en) * 2004-08-02 2007-03-15 Univ Florida High aspect ratio metal particles and methods for forming same
JP2008001974A (en) * 2006-03-31 2008-01-10 Dowa Holdings Co Ltd Silver powder and method for producing the same
JP2014101531A (en) * 2012-11-16 2014-06-05 Nagoya Univ Method for producing nano fluid
CN106660131A (en) * 2014-06-16 2017-05-10 国立大学法人大阪大学 Method for synthesizing silver particles, silver particles, method for manufacturing electroconductive paste, and electroconductive paste
JPWO2015194536A1 (en) * 2014-06-16 2017-05-18 国立大学法人大阪大学 Method for synthesizing silver particles, silver particles, method for producing conductive paste, and conductive paste
US10201852B2 (en) 2014-06-16 2019-02-12 Osaka University Silver particle synthesizing method, silver particles, conductive paste producing method, and conductive paste

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