JPS5896802A - Production of fine metallic powder by wet reduction - Google Patents
Production of fine metallic powder by wet reductionInfo
- Publication number
- JPS5896802A JPS5896802A JP19613681A JP19613681A JPS5896802A JP S5896802 A JPS5896802 A JP S5896802A JP 19613681 A JP19613681 A JP 19613681A JP 19613681 A JP19613681 A JP 19613681A JP S5896802 A JPS5896802 A JP S5896802A
- Authority
- JP
- Japan
- Prior art keywords
- nickel
- copper
- powder
- metallic
- soln
- 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
Links
Classifications
-
- 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
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/16—Making metallic powder or suspensions thereof using chemical processes
- B22F9/18—Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds
- B22F9/20—Making metallic powder or suspensions thereof using chemical processes with reduction of metal compounds starting from solid metal compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は1ミクロン以下の微細な金属ニッケル粉、及
び金属銅粉を湿式還元で製造する方法に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing fine metallic nickel powder of 1 micron or less and metallic copper powder by wet reduction.
これ等金属の粉末を製造する従来の方法には、電解法及
び水素還元法、熱分解法、熔融噴射法、ガス中蒸発法等
の所■乾式法があるが、すべて、煩雑な設備と高度の技
術を必要とする。これらに比べ、湿式還元は最も手がる
で且つ簡単な設備ですむが、従来の湿式還元法で1ミク
ロン以下の金属粉末を得るには、密閉容器での加圧を必
要としたり、或は高価な還元剤を大量に使用したりしな
ければばらない。Conventional methods for manufacturing these metal powders include dry methods such as electrolytic method, hydrogen reduction method, pyrolysis method, melt injection method, and evaporation method in gas, but all of them require complicated equipment and advanced technology. technology is required. Compared to these methods, wet reduction is the most convenient and requires the simplest equipment, but in order to obtain metal powder of 1 micron or less using conventional wet reduction methods, pressurization in a closed container is required, or It is necessary not to use large amounts of expensive reducing agents.
本法は、これ等の欠点を除去し、簡単な設備で確実に、
且つ安全に1ミクロン以下の金属ニッケル及び銅の微粉
末を製造せんとするものである。This method eliminates these drawbacks and reliably uses simple equipment.
Moreover, it is intended to safely produce metallic nickel and copper fine powders of 1 micron or less.
すなわち、本法では、ニッケル及び銅の化合物として最
も入手し易い硫酸ニッケル、及び硫酸銅を溶解した液に
苛性ソーダ又は炭酸ソーダ、或はこれ等の混合液を加え
て、水酸化物又は炭酸塩の型で該金属を含有hした粒子
を祈出させる。従って、きわめて細い粒子がこの段階で
生成する。粒子の細かさは液の濃度が最も影響し通常濃
度が低い程祈出粒子は細くなる。That is, in this method, caustic soda, soda carbonate, or a mixture thereof is added to a solution in which nickel sulfate and copper sulfate, which are the most easily available nickel and copper compounds, are dissolved, and hydroxide or carbonate is dissolved. Particles containing the metal are poured into a mold. Therefore, very fine particles are produced at this stage. The fineness of the particles is most influenced by the concentration of the liquid, and normally the lower the concentration, the thinner the particles will be.
次に、還元剤としては、ヒドラジン又はヒドラジンヒド
ラートを3〜8当量使用したが、これは3当量以下では
反応が長くかかるから或は不安定なためで、また経済性
の点から8当量程度で押えたまでである。還元剤点火後
撹拌しながら加熱すると、反応は液の濃度、還元剤添加
当量等によって異なるが、ニッケルの場合70〜90℃
で反応を開始して温度の上昇と共にはげしさを増し、反
応完了■■■する。銅の場合はもっと低温より反応が始
まるが、この段階では弱く、最終的には85℃以上のは
げしい反応でないと完全な金属銅にならない。Next, as a reducing agent, hydrazine or hydrazine hydrate was used in an amount of 3 to 8 equivalents, but this is because if the amount is less than 3 equivalents, the reaction will take a long time or is unstable, and from the economic point of view, about 8 equivalents are used. I was able to hold it down. When heated while stirring after igniting the reducing agent, the reaction will vary depending on the concentration of the liquid, the equivalent amount of reducing agent added, etc., but in the case of nickel, the reaction temperature will be 70 to 90°C.
The reaction starts and becomes more vigorous as the temperature rises until the reaction is complete. In the case of copper, the reaction begins at a much lower temperature, but it is weak at this stage, and complete metallic copper cannot be produced until the final reaction is violent at temperatures above 85°C.
いずれの場合も反応終了すると気泡は弱まり、液が透明
になる。次いで静置、冷却すると金属粉は沈殿するので
、上質塩を流し、水洗を数回行ない濾過後乾燥して製品
とする。乾燥は酸化防止のため、なるべく真空乾燥がよ
く、特に銅は酸化され易いので注意しなければならない
。In either case, once the reaction is complete, the bubbles weaken and the liquid becomes transparent. When the metal powder is then left to stand and cooled, it precipitates, so high-quality salt is poured over it, washed with water several times, filtered, and dried to obtain a product. To prevent oxidation, vacuum drying is preferable, and care must be taken especially since copper is easily oxidized.
次に実施例に従って説明する。Next, an explanation will be given according to an example.
実施例(1)
硫酸ニッケル(NiSO4、5H2O)500gを1l
の水に溶かし、中和剤としては苛性ソーダ(NaOH)
150gを1lの水に溶解した。この両液を撹拌しなが
ら混合すると、水酸化ニッケルが直ちに祈出してけんだ
くした。このけんだく液に60%のヒドラジンヒドラー
トを450ml加えてよく撹拌しながら加熱したところ
、80℃を超したところで急激な反応が始まり、気泡が
盛んに立ち始めたため、加熱を弱めてあふれるのを防ぎ
つつ反応させたところ、88℃で反応は継続し、約1時
間して、液は無色になり、気泡の発生も止った・静置し
てニッケル粉を沈め、上澄液を流し、数回デカンテーシ
ョンを行ない水洗し、最後にアセトンで洗って濾過、減
圧乾燥した。Example (1) 1 liter of 500 g of nickel sulfate (NiSO4, 5H2O)
Dissolve in water and use caustic soda (NaOH) as a neutralizing agent.
150 g was dissolved in 1 liter of water. When these two solutions were mixed with stirring, nickel hydroxide immediately started to form and swell. When 450 ml of 60% hydrazine hydrate was added to this suspension and heated while stirring well, a rapid reaction started when the temperature exceeded 80°C and bubbles started to form, so the heating was weakened to prevent overflowing. The reaction continued at 88°C, and after about 1 hour, the liquid became colorless and the generation of bubbles stopped.The nickel powder was allowed to stand still, and the supernatant liquid was poured off. It was decanted twice, washed with water, and finally washed with acetone, filtered, and dried under reduced pressure.
この様にして得られたニッケル粉は、約110gであっ
た。また電子顕微鏡で調べた結果、粒経は0.7ミクロ
ンであった。The nickel powder thus obtained weighed about 110 g. Further, as a result of examination using an electron microscope, the grain size was 0.7 microns.
実施例(2)
硫酸ニッケル500gを3lの水に溶かし、中和剤には
苛性ソーダ101gと炭酸ソーダ(NO4CO3)67
gを1lの水に溶かした液を使用し、還元剤その他実施
例(1)と同様にしたところ、還元は92℃で維持した
。出来たニッケル粉の粒経は0.3ミクロンであった。Example (2) Dissolve 500 g of nickel sulfate in 3 liters of water, and use 101 g of caustic soda and 67 g of soda carbonate (NO4CO3) as neutralizing agents.
Using a solution prepared by dissolving 1.5 g in 1 liter of water, the same reducing agent and other methods as in Example (1) were used, and the reduction was maintained at 92°C. The particle size of the resulting nickel powder was 0.3 microns.
実施例(3)
硫酸銅(C12SO4・5H2O)500gを1.5l
の水に溶かした液と、苛性ソーダ160gを2lの水に
溶かした液とを混合して、水酸化銅の微粒子を祈出させ
、充分撹拌混合してから60%ヒドラジンヒドラート4
50mlを加えて撹拌加熱したところ、50℃から気泡
が出て反応が始まり、90℃を超すと反応は更に盛んに
なり、加熱を始めてから65分で完了した。Example (3) 500g of copper sulfate (C12SO4.5H2O) to 1.5L
A solution of 160 g of caustic soda dissolved in 2 liters of water was mixed with a solution of 160 g of caustic soda dissolved in 2 liters of water to extract fine particles of copper hydroxide, and after thorough stirring and mixing, 60% hydrazine hydrate 4
When 50 ml of the mixture was added and heated with stirring, the reaction started with bubbles appearing at 50°C, and when the temperature exceeded 90°C, the reaction became more active and was completed in 65 minutes from the start of heating.
静置後沈降した銅粉は、よく洗浄し、濾過後真空乾燥し
た。銅粉の粒経は0.2ミクロンであった。The copper powder that settled after standing was thoroughly washed, filtered, and then vacuum dried. The grain size of the copper powder was 0.2 microns.
実施例(4)
実施例(3)の苛性ソーダを炭酸ソーダ215gに■え
、他は実施例(3)同様に行なった。Example (4) The same procedure as in Example (3) was carried out except that the caustic soda of Example (3) was added to 215 g of soda carbonate.
反応は85℃を超すとはげしくなったが、反応時間は、
加熱を始めてから45分で完了した。The reaction became more rapid when the temperature exceeded 85°C, but the reaction time was
Heating was completed in 45 minutes after starting.
銅粉の粒経は、0.3ミクロンであった。The grain size of the copper powder was 0.3 microns.
以上の如く本法は、従来の湿式還元と異なり、液相から
直接金属を還元祈出するのではなく、先ず中和によって
、金属の水酸化化合物或は炭酸塩の微粒子を祈出させる
ので、非常に細かい粒子とすることが出来、従ってこれ
を還元した金属粒子は更に細いものとして得られる。ま
た静置も通常の撹拌槽と加熱装置が生体で、特別なもの
はいらず、常圧反応で充分である。As mentioned above, unlike conventional wet reduction, this method does not directly reduce the metal from the liquid phase, but first removes fine particles of the metal hydroxide compound or carbonate through neutralization. It can be made into very fine particles, and therefore the metal particles obtained by reducing it can be obtained as even finer particles. Furthermore, for the purpose of standing still, a normal stirring tank and heating device are used for the living body, no special equipment is required, and a normal pressure reaction is sufficient.
即ち本法によれば、工業的に入手し易い、硫酸ニッケル
及び硫酸銅を原料とし、極めて簡単な設備と操作で1ミ
クロン以下の金属ニッケル及び金属銅の微粉を製造する
ことが可能です。In other words, according to this method, it is possible to produce fine powders of metallic nickel and metallic copper of 1 micron or less using extremely simple equipment and operations using industrially easily available nickel sulfate and copper sulfate as raw materials.
Claims (1)
するに当り、該金属含有溶液に苛性ソーダ、又は炭酸ソ
ーダの溶液、或は両者混合溶液を加えて、ニッケル或は
銅の水酸化物、又は炭酸塩の微細な沈殿或はコロイド粒
子を祈出させて後、還元することを特徴とする微細ニッ
ケル粉及び銅粉の製造方法。When producing the metal fine powder from a nickel or copper sulfate solution, a solution of caustic soda or soda carbonate, or a mixed solution of both is added to the metal-containing solution to form a hydroxide of nickel or copper. A method for producing fine nickel powder and copper powder, characterized by reducing the fine precipitates or colloidal particles of carbonate or carbonate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19613681A JPS5896802A (en) | 1981-12-04 | 1981-12-04 | Production of fine metallic powder by wet reduction |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19613681A JPS5896802A (en) | 1981-12-04 | 1981-12-04 | Production of fine metallic powder by wet reduction |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5896802A true JPS5896802A (en) | 1983-06-09 |
Family
ID=16352830
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19613681A Pending JPS5896802A (en) | 1981-12-04 | 1981-12-04 | Production of fine metallic powder by wet reduction |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5896802A (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6086203A (en) * | 1983-10-15 | 1985-05-15 | Fukuda Kinzoku Hakufun Kogyo Kk | Preparation of fine copper powder |
JPS6299406A (en) * | 1985-10-28 | 1987-05-08 | Mitsui Mining & Smelting Co Ltd | Production of copper powder |
JPH04195293A (en) * | 1990-11-24 | 1992-07-15 | Fuji Electric Co Ltd | Raw material output device for cup type automatic vending machine |
US5741347A (en) * | 1995-02-24 | 1998-04-21 | Murata Manufacturing Co., Ltd. | Method for producing copper powder |
EP0908258A2 (en) * | 1997-09-11 | 1999-04-14 | MITSUI MINING & SMELTING CO., LTD. | Method for preparing nickel fine powder |
JP2013053365A (en) * | 2011-08-09 | 2013-03-21 | Osaka Gas Co Ltd | Method for manufacturing metallic particle utilizing solvothermal reaction |
US9371343B2 (en) | 2009-12-18 | 2016-06-21 | Invista North America S.A. R.L. | Nickel metal compositions and nickel complexes derived from basic nickel carbonates |
JP2017222531A (en) * | 2016-06-14 | 2017-12-21 | 住友金属鉱山株式会社 | Nickel hydroxide particles, method for producing the same, and method for producing nickel oxide fine powder using the same |
JP2018024550A (en) * | 2016-08-10 | 2018-02-15 | 住友金属鉱山株式会社 | Nickel oxide fine powder and production method of the same |
JP2020121923A (en) * | 2020-04-24 | 2020-08-13 | 住友金属鉱山株式会社 | Nickel hydroxide particle |
JP2020186171A (en) * | 2020-07-28 | 2020-11-19 | 住友金属鉱山株式会社 | Nickel hydroxide particle |
-
1981
- 1981-12-04 JP JP19613681A patent/JPS5896802A/en active Pending
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6086203A (en) * | 1983-10-15 | 1985-05-15 | Fukuda Kinzoku Hakufun Kogyo Kk | Preparation of fine copper powder |
JPS6299406A (en) * | 1985-10-28 | 1987-05-08 | Mitsui Mining & Smelting Co Ltd | Production of copper powder |
JPH0557324B2 (en) * | 1985-10-28 | 1993-08-23 | Mitsui Mining & Smelting Co | |
JPH04195293A (en) * | 1990-11-24 | 1992-07-15 | Fuji Electric Co Ltd | Raw material output device for cup type automatic vending machine |
US5741347A (en) * | 1995-02-24 | 1998-04-21 | Murata Manufacturing Co., Ltd. | Method for producing copper powder |
EP0908258A3 (en) * | 1997-09-11 | 2000-02-23 | MITSUI MINING & SMELTING CO., LTD. | Method for preparing nickel fine powder |
EP0908258A2 (en) * | 1997-09-11 | 1999-04-14 | MITSUI MINING & SMELTING CO., LTD. | Method for preparing nickel fine powder |
US6120576A (en) * | 1997-09-11 | 2000-09-19 | Mitsui Mining And Smelting Co., Ltd. | Method for preparing nickel fine powder |
US9371343B2 (en) | 2009-12-18 | 2016-06-21 | Invista North America S.A. R.L. | Nickel metal compositions and nickel complexes derived from basic nickel carbonates |
JP2013053365A (en) * | 2011-08-09 | 2013-03-21 | Osaka Gas Co Ltd | Method for manufacturing metallic particle utilizing solvothermal reaction |
JP2017222531A (en) * | 2016-06-14 | 2017-12-21 | 住友金属鉱山株式会社 | Nickel hydroxide particles, method for producing the same, and method for producing nickel oxide fine powder using the same |
JP2018024550A (en) * | 2016-08-10 | 2018-02-15 | 住友金属鉱山株式会社 | Nickel oxide fine powder and production method of the same |
JP2020121923A (en) * | 2020-04-24 | 2020-08-13 | 住友金属鉱山株式会社 | Nickel hydroxide particle |
JP2020186171A (en) * | 2020-07-28 | 2020-11-19 | 住友金属鉱山株式会社 | Nickel hydroxide particle |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS5896802A (en) | Production of fine metallic powder by wet reduction | |
WO2016202271A1 (en) | Method of recovering rare earth, aluminum and silicon from rare earth-containing aluminum-silicon scraps | |
BR112014021852B1 (en) | PROCESS FOR RECOVERY OF COBALT, RUTENUM AND ALUMINUM METALS FROM CO-RU / AL²O³ CATALYST WASTE IN FISCHER-TROPSCH SYNTHESIS | |
US3201223A (en) | Method of preparation of silver powder having a protective gum coating | |
CN106029270A (en) | Method for producing nickel powder | |
US3334995A (en) | Process of precipitating silver | |
DE2222173C3 (en) | Process for the production of metals or metal alloys | |
US3273997A (en) | Wet process for the separation, isolation, and recovery of certain metallic and non-metallic constituents of waste slag from reverberatory refining of copper pyritic type ores | |
JPS63125605A (en) | Production of fine metal powder | |
US1955326A (en) | Process for the manufacture of chromates and dichromates | |
NO161130B (en) | PROCEDURE FOR THE PREPARATION OF A DOUBLE COBOLT POWDER WITH A ROUGH, RELATIVE UNIFORM PARTICLE SIZE. | |
CN113215404B (en) | Method for preparing spherical cobaltosic oxide from cobalt-ammonia complex solution | |
JP2621915B2 (en) | Method for producing ultrafine copper powder | |
US3717481A (en) | Gold metallizing compositions | |
US2912305A (en) | Non-ferrous scrap treatment | |
JPH10183208A (en) | Production of silver powder | |
US3288597A (en) | Process for the recovery of certain metallic and non-metallic constituents of waste slag from reverberatory refining of copper pyritic type ores | |
US1262062A (en) | Method of utilizing aluminum skimmings and analogous material. | |
JPH07177B2 (en) | Method for producing catalyst for methanol steam reforming | |
US1067698A (en) | Method of electrolytically recovering nickel. | |
US3806591A (en) | Preparation of group viii metal compounds | |
JPS59174522A (en) | Manufacture of fine dispersion of metal oxide and/or metal hydroxide in aluminum hydroxide | |
US2201508A (en) | Manufacture of zirconium compounds | |
JPH0249364B2 (en) | ||
US1232334A (en) | Process of separating thorium from soda solutions containing thorium oxalate. |