JPS61276905A - Production of fine silver particle - Google Patents

Production of fine silver particle

Info

Publication number
JPS61276905A
JPS61276905A JP11799885A JP11799885A JPS61276905A JP S61276905 A JPS61276905 A JP S61276905A JP 11799885 A JP11799885 A JP 11799885A JP 11799885 A JP11799885 A JP 11799885A JP S61276905 A JPS61276905 A JP S61276905A
Authority
JP
Japan
Prior art keywords
soln
aqueous
silver nitrate
silver
particle size
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
JP11799885A
Other languages
Japanese (ja)
Inventor
Hiroshi Tamemasa
博史 為政
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.)
Tanaka Kikinzoku Kogyo KK
Original Assignee
Tanaka Kikinzoku Kogyo KK
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 Tanaka Kikinzoku Kogyo KK filed Critical Tanaka Kikinzoku Kogyo KK
Priority to JP11799885A priority Critical patent/JPS61276905A/en
Publication of JPS61276905A publication Critical patent/JPS61276905A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To produce fine silver particles having a narrow particle size distribution when the aqueous soln. of an ammoniac silver nitrate complex is reduced with glucose in a hydrophobic reaction vessel to produce fine silver particles, by adding a nonionic surfactant to the reactive soln. CONSTITUTION:The aqueous soln. of glucose as a reducing agent is poured into a reaction vessel after the inside of the vessel is made hydrophobic by oil coating or other method, and a nonionic surfactant such as 'Esomide(R)' or 'Esofat(R)' is added to the soln. and stirred. The aqueous soln. of an ammoniac silver nitrate complex prepd. by adding an aqueous ammonia soln. to an aqueous silver nitrate soln. is slowly added to the soln. in the reaction vessel to reduce the silver nitrate complex with the glucose. Singly dispersed fine silver particles having a narrow particle size distribution are obtd. without causing flocculation.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は微細な銀粒子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 fine silver particles.

(従来技術とその問題点) 従来、銀微粒子の製造方法としては疎水性反応槽内てa
死刑としてブドウ糖を用いてアンモニア性硝酸銀↑(1
体)容器を還元する方法が用いられてきた。ところが、
この方法は析出した彷l!粒子同志が引き寄−已合って
凝集し、粒度分布の幅の広い銀粒子しか得られないとい
う欠点を有していた。
(Prior art and its problems) Conventionally, as a method for producing fine silver particles, a
Ammoniacal silver nitrate ↑ (1
A method of reducing the container (body) has been used. However,
This method is a great success! This method has the drawback that the particles are attracted to each other and aggregate, resulting in silver particles having only a wide particle size distribution.

(発明の目的) 本発明は−1−記の欠点を解消せんがためになされたも
のであり、分11シした粒度分布の幅の狭い微細な銀粒
子の製造方法をbE ’0’、−1んとするものである
(Objective of the Invention) The present invention has been made in order to eliminate the drawbacks listed in -1-, and provides a method for producing fine silver particles with a narrow particle size distribution of bE '0', - 1.

(問題点を解決するための手段) 本発明は疎水性反応槽内て還元剤を用いて、アンモニア
性硝酸銀↑(1体溶液を還元して銀微粒子を製造する方
法において、反応溶液中にノニオン系界面活性剤を添加
することによって1y分散した銀微粒子を得ることを特
徴とするものである。
(Means for Solving the Problems) The present invention uses a reducing agent in a hydrophobic reaction tank to produce silver particles by reducing an ammoniacal silver nitrate ↑ (one-body solution). This method is characterized by obtaining 1y-dispersed silver fine particles by adding a surfactant.

そして、本発明の製造方法において反応槽内面を疎水性
に保つ理由は、71表水性の場合、析出反応が容器の壁
で起きるため、凝集した才′)度分布の幅の広い銀粒子
しか得られないが、反応槽内面を疎水性に保つことによ
って析出反応を水溶液中で均一に起こすことができるよ
うになるからである。
The reason why the inner surface of the reaction tank is kept hydrophobic in the production method of the present invention is that in the case of 71 surface water, the precipitation reaction occurs on the wall of the container, so only silver particles with a wide range of agglomerated crystallinity distribution are produced. However, by keeping the inner surface of the reaction tank hydrophobic, the precipitation reaction can occur uniformly in the aqueous solution.

また、反応溶液中にカチオン系界面活性剤を添加する理
由は、アンモニア性硝酸銀↑(1体溶液を還元すること
によって、水溶液中に析出した銀微粒子が凝集しないで
中4分11シ状態を保つようにずろためである。
In addition, the reason for adding a cationic surfactant to the reaction solution is that by reducing the ammoniacal silver nitrate ↑ (one-body solution), the silver fine particles precipitated in the aqueous solution do not aggregate and maintain the medium state. It's because of the difference.

本発明において反応槽内面を疎水性に保つ方法としては
、オイルコーティング、界面活性剤コーティング、テフ
ロンコーティング等であり、反応溶液中に添加するノニ
オン系界面活性剤としてはエソマイト、エソフγソ1、
ザーフロンS −14,1ザ−フロンS −145等で
ある。
In the present invention, methods for keeping the inner surface of the reaction tank hydrophobic include oil coating, surfactant coating, Teflon coating, etc. Nonionic surfactants added to the reaction solution include Esomite, Esof γ So1,
These include Zaflon S-14, 1 Zaflon S-145, etc.

ここで、本発明の実施例について説明する。Examples of the present invention will now be described.

(実施例1) ブドウtJIW 50 gを50°Cの水300m+8
に熔解し、この溶液にノニオン系界面活性剤エソマイ[
を1.2 m (l添加してテフロンコーティングした
ビーカー中で攪拌しておく。また、別のビーカーてfi
l“j酸銀1. Ogを20mAの水乙こ熔解し、これ
に28%アンモニア水8mpを加えてアン干ニア性硝酸
8N 1g体溶液とし、これを先のブドウ糖+エソマイ
ト溶液中に徐々に添加する。得られた銀微粒子iftデ
カンチーシコンにより充分に水で洗浄して、粒度分布測
定及び電子顕微鏡観察を行なった。
(Example 1) 50 g of grape tJIW was added to 300 m of water at 50°C +8
and add the nonionic surfactant Esomy to this solution.
Add 1.2 m (l) of water and stir in a Teflon-coated beaker.
Melt 1.0 g of silver acid at 20 mA in water, add 8 mp of 28% ammonia water to make a solution of 1 g of 8N ammonia nitric acid, and gradually add this to the glucose + esomite solution. The obtained silver particles were thoroughly washed with water and subjected to particle size distribution measurement and electron microscopic observation.

その結果、この銀微粒子は平均粒径1.5 t!mで粒
度分布は図のように幅の)ノニい4)ので、形状はほぼ
fF、形て分散したものてあ−2た。
As a result, the average particle size of these silver particles was 1.5 tons! As shown in the figure, the particle size distribution was wide (as shown in the figure), so the shape was approximately fF, and the shape was dispersed.

(実施例2) ブドウ1I7i 100 、、を50 ’r:の水50
0mplこン1゛ζ解し、この溶液にノニオン系界面活
+41剤、−り゛−フロンS−1/IIを0.7 rn
ρ添加してシリ:1−ンオイルコーティングしたビーカ
ーの中で攪拌して」9く。また、別のビーカー中で硝酸
銀25gを50m1.の水に溶解し、ごれに28%アン
モニア水20m1を加えてアンモニア性硝酸1門11体
溶液とし、これを先のフ゛トつ本1iH→−“リーーフ
11ンS−141/lン1奴中に徐々々に添加する。1
ゴられた銀微粒子も31′デカンテーシヨンにより充分
に水で’tjI= ?’/’ シて、1′)”L度分布
測定及び電子顕/、5鏡観察を行った。
(Example 2) Grape 1I7i 100, 50'r: water 50
Dissolve 0 ml of this solution and add 0.7 rn of nonionic surfactant +41 agent and -Ri-Freon S-1/II to this solution.
Add ρ and stir in a beaker coated with silicone oil. Also, in a separate beaker, 50 ml of 25 g of silver nitrate was added. of water, add 20ml of 28% ammonia water to the dirt to make an ammoniacal nitric acid solution. Gradually add to 1.
The crushed silver particles are also thoroughly soaked with water by 31' decantation. 1')"L power distribution measurement and electron microscopy/5 mirror observation were performed.

その結果、この銀微粒子は丁均才′◇径0.9 tt 
mで、粒度分布は図のように幅の狭いもので形状はほぼ
球形で単分散したものであった。
As a result, these fine silver particles had a diameter of 0.9 tt.
m, the particle size distribution was narrow as shown in the figure, and the shape was almost spherical and monodisperse.

(従来例) フ゛トウ!Fi 70 gを50℃の水400m4に?
8角了し、この溶液をテフロンコーティングしたビーカ
一中で1景拌しておく。また別のビーカー中で硝酸1尺
15gを30mffの水に?容解し、これに28%アン
モニア水13mnを加えてアンモニア性硝酸銀銘体溶液
とし、これを先のブドウIJ、’i溶液中に徐々に添加
する。得られた銀粒子はデカンテーションにより充分に
水で洗浄して、粒度分布測定及び電子顕微鏡観察を行っ
た。
(Conventional example) Fight! 70 g of Fi in 400 m4 of water at 50℃?
After 8 hours, stir this solution in a Teflon-coated beaker. In another beaker, add 15g of nitric acid to 30mff of water? Dissolve and add 13 ml of 28% ammonia water to obtain an ammoniacal silver nitrate solution, which is gradually added to the grape IJ,'i solution. The obtained silver particles were thoroughly washed with water by decantation, and subjected to particle size distribution measurement and electron microscopic observation.

その結果、この銀粒子II平均粒径5,2μmで粒度分
布は図のように幅の広い擬集したものであった。
As a result, the average particle diameter of the silver particles II was 5.2 μm, and the particle size distribution was agglomerated with a wide range as shown in the figure.

(発明の効果) 上記の説明で明らかなように本発明の製造方法は疎水性
反応槽内で還元剤を使用して、アンモニア性硝酸銀錯体
溶液を還元して銀微粒子を製造する方法に於いて、反応
溶液中にノニオン系界面活性剤を添加することにより、
従来法では得られなかった単分散した粒度分布の狭いi
故細な銀粒子を製造できるので、従来の製造法にとって
代わることのできる画jjJl的なものと言える。
(Effects of the Invention) As is clear from the above explanation, the production method of the present invention is a method for producing silver fine particles by reducing an ammoniacal silver nitrate complex solution using a reducing agent in a hydrophobic reaction tank. , by adding a nonionic surfactant to the reaction solution,
Monodisperse and narrow particle size distribution that cannot be obtained with conventional methods
Since it is possible to produce fine silver particles, it can be said to be a method that can replace conventional production methods.

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

図は光透過式粒度分布測定装置を用いて各銀i故粒子の
1′1j度分布を測定した結果を横軸に粒径、81子軸
に累積パーセントを取って示したものである。
The figure shows the results of measuring the 1'1j degree distribution of each silver i particle using a light transmission type particle size distribution measuring device, with the horizontal axis representing the particle diameter and the 81 minor axis representing the cumulative percentage.

Claims (1)

【特許請求の範囲】[Claims] 疎水性反応槽内で還元剤を用いてアンモニア性硝酸銀錯
体溶液を還元して銀微粒子を製造する方法に於いて、反
応溶液中にノニオン系界面活性剤を添加することによっ
て単分散した銀微粒子を得ることを特徴とする銀微粒子
の製造方法。
In a method for producing silver fine particles by reducing an ammoniacal silver nitrate complex solution using a reducing agent in a hydrophobic reaction tank, monodispersed silver fine particles are produced by adding a nonionic surfactant to the reaction solution. A method for producing fine silver particles, characterized in that:
JP11799885A 1985-05-31 1985-05-31 Production of fine silver particle Pending JPS61276905A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11799885A JPS61276905A (en) 1985-05-31 1985-05-31 Production of fine silver particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11799885A JPS61276905A (en) 1985-05-31 1985-05-31 Production of fine silver particle

Publications (1)

Publication Number Publication Date
JPS61276905A true JPS61276905A (en) 1986-12-06

Family

ID=14725509

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11799885A Pending JPS61276905A (en) 1985-05-31 1985-05-31 Production of fine silver particle

Country Status (1)

Country Link
JP (1) JPS61276905A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6425910A (en) * 1987-04-07 1989-01-27 Norddeutsche Affinerie Production of non-ferrous metal powder or non-ferrous metal powder mixture
JP2000129318A (en) * 1998-10-22 2000-05-09 Dowa Mining Co Ltd Silver powder and its production
US6660058B1 (en) * 2000-08-22 2003-12-09 Nanopros, Inc. Preparation of silver and silver alloyed nanoparticles in surfactant solutions
CN103785853A (en) * 2014-01-24 2014-05-14 太原理工大学 Preparation method of hybrid carbon silver composite material

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6425910A (en) * 1987-04-07 1989-01-27 Norddeutsche Affinerie Production of non-ferrous metal powder or non-ferrous metal powder mixture
JP2000129318A (en) * 1998-10-22 2000-05-09 Dowa Mining Co Ltd Silver powder and its production
US6660058B1 (en) * 2000-08-22 2003-12-09 Nanopros, Inc. Preparation of silver and silver alloyed nanoparticles in surfactant solutions
CN103785853A (en) * 2014-01-24 2014-05-14 太原理工大学 Preparation method of hybrid carbon silver composite material

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