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JPH058242B2 - - Google Patents
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JPH058242B2 - - Google Patents

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Publication number
JPH058242B2
JPH058242B2 JP59202185A JP20218584A JPH058242B2 JP H058242 B2 JPH058242 B2 JP H058242B2 JP 59202185 A JP59202185 A JP 59202185A JP 20218584 A JP20218584 A JP 20218584A JP H058242 B2 JPH058242 B2 JP H058242B2
Authority
JP
Japan
Prior art keywords
chloride
iron powder
copper
powder
solution
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.)
Expired - Fee Related
Application number
JP59202185A
Other languages
Japanese (ja)
Other versions
JPS6179707A (en
Inventor
Hideo Uehara
Shohei Kosaka
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.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials Corp
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 Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP59202185A priority Critical patent/JPS6179707A/en
Publication of JPS6179707A publication Critical patent/JPS6179707A/en
Publication of JPH058242B2 publication Critical patent/JPH058242B2/ja
Granted legal-status Critical Current

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  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)
  • Powder Metallurgy (AREA)

Description

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

〔産業上の利用分野〕 この発明は、粉末冶金用鉄粉の表面に銅を容易
に被覆することができる粉末冶金用の銅被覆鉄粉
の製法に関するものである。 〔従来の技術〕 粉末冶金用の鉄−銅燒結合金用材料として従来
から使用されている形態には合金粉、又は混合粉
が挙げられる。 この様な金属粉として、合金粉を燒結合金材料
として使用した場合は、アトマイズ法等により鉄
−銅合金粉として製造されるために、粒子の均一
性については優れているが、粒子の硬度が高いた
めに成型性が悪いという欠点を有している。 また、混合粉を使用した場合には、均一な混合
が技術的に難しく、粒子の大きさ並びに形状等に
影響されて、粉末粒子が粗い程偏折を生じ易く、
且つ燒結寸法のバラツキが増大する。 これらの欠点を排除するために、種々の銅被覆
鉄粉の製造方法が提案されている。 例えば、粉末冶金用鉄粉と金属銅、酸化銅又は
還元性銅化合物の微粉を混合した後に還元性雰囲
気中で加熱処理して、鉄粉表面上に金属銅微粒子
を被覆する方法等があげられるが、均一な混合が
必要である点、並びに加熱処理により被覆粒子の
一部に合金化が進み、粒子の硬度が高くなるため
に圧縮性や成形性等に悪い影響を及ぼす。 また、銅原料としての金属銅、酸化銅や還元性
銅化合物の粒子と、鉄粉粒子との粒子径の選択と
配合バランスの選定が難しく、その選定が不適で
あると鉄粒子と銅粒子との付着性が著しく低下す
る虞れがある。 また、湿式法として銅塩類水溶液中に鉄粉を浸
漬し、イオン化傾向の差で金属鉄と銅イオンを置
換することによつて鉄粉表面上を金属銅で被覆す
る方法もあり、かゝる銅塩類の水溶液として硫酸
銅、塩化第二銅の使用を挙げることができる。 しかし、硫酸銅の使用は硫酸銅溶液中では2価
の銅イオンと金属鉄との化学的な置換反応である
ため、多量の金属鉄が水溶液中へ第一鉄イオンと
して溶出する。それ故、鉄粉表面上に被覆した金
属銅と当量の鉄粉を損失することになり、その鉄
の溶出量だけ、製品のコスト高になる。また、鉄
粉の形状を金属鉄の溶出により変化させることで
燒結体の強度を著しく低下させる欠点もある。 さらに、塩化第二銅溶液を使用した場合には、
硫酸銅溶液を使用した場合と同様な問題点ももち
ろん考えられるが、鉄粉末表面上に均一な金属銅
微粒子が被覆されるのではなく、不均一で且つ付
着性の悪いデンドライト状にのびた銅が被覆され
るため、従来の方法と比較して製造された銅被覆
鉄粉は流動性も悪く、また、成形性、燒結体の機
械的特性等を向上させることができない。 〔発明が解決しようとする問題点〕 合金粉、混合粉及び銅被覆鉄粉等の従来技術に
は一長一短があるが、特に銅被覆鉄粉に関し、前
記の硫酸銅や塩化第二銅溶液を使用した場合より
も金属鉄の溶出が少なく、且つ付着性の良い金属
銅微粒子を鉄粉表面に均一に被覆することができ
れば、粉末冶金材料としての有用性を高めること
ができる。 また、かゝる条件を満たした上で被覆すべき銅
の原料として各種のエツチング廃液を利用するこ
とができれば、より安価な粉末冶金用の材料を得
ることができる。 この発明はかゝる問題に取り組んで研究の結果
完成されたものである。 〔問題点を解決するための手段〕 この発明は、アトマイズ粉、還元粉等の粉末冶
金用鉄粉を使用し、かつ金属材料のエツチングで
生成した塩化第二銅を主成分とするエツチング廃
液、又は塩化第二鉄を主成分とするエツチング廃
液より還元して作られた塩化第一鉄溶液又は/及
び塩化ナトリウム溶液に塩化第一銅が溶解した液
を作り、この液の中に前記粉末冶金用鉄粉を浸漬
して塩化第一銅を原料として化学的な置換方法に
よつて金属銅微粒子を鉄粉表面に均一に被覆する
ものである。 より具体的には、塩化第二銅を主成分とするエ
ツチング廃液に金属銅を加え、その中の塩化第二
銅を還元せしめた塩化第一銅を、塩化第一鉄溶液
又は/及び塩化ナトリウム溶液に溶解せしめてな
る反応液に、粉末冶金用鉄粉を浸漬し、該鉄粉の
表面を金属銅により被覆することを特徴とする銅
被覆鉄粉の製法である。 この発明において、実際に粉末冶金用鉄粉に被
覆される銅の原料となるものは塩化第一銅で、こ
の塩化第一銅は塩化第一鉄の溶液に溶解して得ら
れた反応液である。 この銅原料となる塩化第一銅は水に対する溶解
度が低く、難溶性であるので、塩化第一銅のみを
水に分散しただけでは反応液として使用すること
ができない。 そこで、塩化第一銅が塩化第一鉄溶液、塩化ナ
トリウム溶液等の塩素イオンを多量に含んでいる
溶液中で錯塩を作つて溶解する性質を利用し、こ
れを反応液として、前述の塩化第二銅の単独溶液
を反応液として用いた場合に生ずる鉄粉表面への
不均一且つ付着性の悪いデンドライト状にのびた
金属銅の被覆の生成を抑制せんとすることを主目
的としたものである。 かゝる抑制効果に関し、塩化第一鉄、または塩
化ナトリウムの濃度が低くなるほど、また反応温
度が高くなるほどデンドライト状の銅付着物の割
合が増す傾向を示す。 したがつて、例えば、反応液として錯塩を形成
する塩化第一銅の入つた塩化第一鉄溶液を使用し
た場合、反応液中の塩化第一鉄の濃度を10%(重
量%;以下同じ)以上、特に15%以上とし、ま
た、塩化ナトリウム溶液を使用した場合の反応液
中の塩化ナトリウム濃度を8%以上、特に10%以
上とすることが好ましく、その反応温度は60℃以
下、特に50℃以下で実施することが望ましい。 反応液中の塩化第一鉄濃度及び塩化ナトリウム
濃度が前記の濃度以下の希薄状態で使用され、ま
たは反応温度が高温に過ぎるときは、鉄粒子表面
へのデンドライト状の金属銅の付着が増す傾向に
あり、これに伴つて銅被覆鉄粉の見掛密度や流動
性も低下する傾向を生じる。 また、塩化第一銅の濃度としては、該塩化第一
銅が溶液中で錯塩を形成して溶解するための適当
な濃度が選ばれる。 これは銅被覆鉄粉の目標となる銅付着量より算
出されるが、一方、反応液中に浸漬した鉄粉を十
分な撹拌下において液と接触させて銅被覆を形成
するための濃度として考慮され、、これらより塩
化第一鉄溶液、塩化ナトリウム溶液のいずれか、
またはその両者を含む溶液に対して塩化第一銅
0.5〜10%の範囲が好適と言える。 上記の様にして得た反応液を撹拌しながらその
中に鉄粉を投入するか、または鉄粉中に反応液を
加えて数十分程度の撹拌を行うことにより、イオ
ン化傾向による化学的な置換反応を行わしめるこ
とができる。 かくして置換反応を終了した液中より金属銅で
被覆された鉄粉を分離し、残存する塩素イオンが
無くなるまでよく水洗いし、分離、乾燥すること
によつて目的とする銅被覆鉄粉を得ることができ
る。 この発明に使用する鉄粉としては、アトマイズ
法、還元法、その他によつて得た粉末状の金属鉄
が使用される。 それら鉄粉の粒径には特に制限はなく、従来の
粉末冶金用鉄粉として使用されている粒径のもの
が用いられる。 ここで、鉄粉表面に被覆する金属銅の量である
が、製品となる銅被覆鉄粉に対し、0.5〜40%の
範囲で金属銅を被覆することが望ましい。前記の
被覆量が0.5%未満の場合には、焼結体としての
製品の機械的な強度の向上が期待できず、また40
%を越えると銅の置換反応で鉄表面に生ずる銅被
覆が厚くなり、これに伴い鉄の溶出が減少し、銅
の析出反応が起こりにくくなる傾向が生じ好まし
くない。 つぎに、この発明では使用する反応液として以
下に述べる各種エツチング廃液を適宜使用するこ
とができる。 すなわち、電子機器材料として使われている銅
プリント配線基板の製造に際しては、エツチング
剤によるエツチングが行われている。 かゝるエツチング剤として塩化第二鉄を主成分
とするエツチング液、または塩化第二銅を主成分
とするエツチング液等が使用されている。したが
つて、銅プリント配線基板の製造に際しては必然
的にこれらの廃液が生ずる。 また、ステンレス、ニツケル、コバルトなどの
金属材料のエツチング液として前記塩化第二鉄を
主成分とする液が使用されており、当然のことな
がら使用に伴つて廃液が生成される。 これらの廃液は、そのエツチングの対象となる
金属により廃液中に存在する金属化合物の組成分
が変わつてくる。例えば、銅プリント配線基板用
の塩化第二鉄を主成分とするエツチング剤より生
じた廃液は金属化合物の主体が塩化第二鉄で、他
に塩化第一鉄、塩化第二銅を含むものであるが、
同じエツチング剤をステンレスやニツケル、鉄な
どのエツチングに用いても前記塩化第二銅の混入
はない。 また、塩化第二銅を主成分とする銅プリント配
線基板用のエツチング剤より生じた廃液は殆ど塩
化第二銅のみで占められた液である。 この発明は、かゝる廃液中の金属成分を有効に
利用するもので、銅プリント配線基板に用いた塩
化第二鉄を主成分とし、塩化第二銅を含むエツチ
ング廃液に金属鉄又は及び金属銅を加えて液中に
残存する塩化第二鉄を塩化第一鉄に、また塩化第
二銅を塩化第一銅にそれぞれ還元し、かゝる塩化
第一鉄、塩化第一銅を使用して前記反応液を得る
ことができる。 また、前述した塩化第二銅を含むか、もしくは
含まない塩化第二鉄を主成分とするエツチング廃
液に金属銅を加えて液中の塩化第二鉄を塩化第一
鉄に還元すると共に、塩化第一銅を生成せしめ、
これらにより反応液を得ることも可能であり、ま
た廃液組成により金属鉄と金属銅の併用によつて
も反応液を得ることができる。 また、前述のとおり塩化第二銅を主成分とする
エツチング液の使用で生じた塩化第二銅を主成分
とするエツチング廃液に金属銅を加えて、残存す
る塩化第二銅を塩化第一銅にまで還元し、これを
塩化第一鉄溶液又は/塩化ナトリウム溶液に溶解
させて反応液とすることができ、かくして得られ
た反応液中に既述のとおり粉末冶金用鉄粉を浸漬
して銅被覆鉄粉を製造することができる。 さらに、この発明においては、粉末冶金用鉄粉
を反応液中に浸漬して、該粉末冶金用鉄粉の表面
に金属銅の被膜を形成するに際に該銅被覆鉄粉を
反応液より濾過して得られた塩化第一鉄溶液を含
む濾液を、前記エツチング液に合流させて、濾液
中の塩化第一鉄を再度有効に利用することもでき
るので、安価に銅被覆鉄粉を製造することができ
る。 なお、塩化第一鉄含有濾液の使用により、循環
系内に塩化第一鉄の蓄積が生じるので、濾液の一
部を系外に抜取つつ実施することが望ましい。 〔作用〕 この発明の方法は、各種エツチング廃液を使用
し、得た塩化第一銅を塩化第一鉄溶液又は/及び
塩化ナトリウム溶液に溶解せしめてなる反応液に
よつて鉄粉表面に金属銅を被覆させるものである
が、本来難溶性の塩化第一銅が、塩化第一鉄溶液
又は/及び塩化ナトリウム溶液中で錯塩を形成し
て溶解性を持ち、イオン化傾向の差によつて鉄粉
表面に金属銅として均一な被覆を形成することが
できる。 〔実施例〕 以下、実施例および比較例を掲げてこの発明を
詳細に説明する。 実施例 1 塩化第二銅を主成分とするエツチング廃液
(CuCl224.0%)1.5に金属銅を加え、塩化第二
銅を塩化第一銅にまで還元し、これを濃度35%の
塩化第一鉄溶液8.5中に加え撹拌し、沈澱を濾
過して第1表に示す反応液に調整した。 ついで、反応液中にアトマイズ鉄粉1.9Kgを投
入し、鉄粉表面に銅微粒子を付着させ目的とする
銅被覆鉄粉2.1Kgを得た。 実施例 2 塩化第二銅を主成分とするエツチング廃液
(CuCl224.0%)1.5に金属銅を加え、塩化第二
銅を塩化第一銅にまで還元し、これを濃度28%の
塩化ナトリウム溶液10中に加え、撹拌し、沈澱
を濾過したのち、第1表に示す反応液に調整し
た。 ついで、反応液中にアトマイズ鉄粉1.9Kgを投
入し、鉄粉表面に銅微粒子を付着させ目的とする
銅被覆鉄粉2.1Kgを得た。 実施例 3 鉄粉表面に銅微粒子を付着させる際に得た濃度
35%の塩化第一鉄含有濾液8.5中に、塩化第二
銅を主成分とするエツチング廃液(CuCl224.0%)
1.5を加え、さらに金属銅を用いて液中の塩化
第二銅を塩化第一銅にまで還元し、濾過して第1
表の反応液を得、この反応液中にアトマイズ鉄粉
1.9Kgを投入し、鉄粉表面上に銅微粒子を付着さ
せて目的の銅被覆鉄粉2.0Kgを得た。 実施例 4 塩化第二鉄を主成分とするエツチング廃液
(FeCl312.9%、FeCl211.5%、CuCl25.1%)10
に金属鉄を加えて残存する塩化第二鉄を塩化第一
鉄に、塩化第二銅を塩化第一銅にそれぞれ還元さ
せ、沈澱を濾過したのち、粉末の塩化第一銅
700gを加え、第1表に記載の反応液を調整した。 ついで、該反応液中にアトマイズ鉄粉2.0Kgを
投入し、鉄粉表面上に銅微粒子を付着させ目的と
する銅被覆鉄粉2.2Kgを得た。 実施例 5 鉄粉表面に銅微粒子を付着させる際に得た濃度
35%の塩化第一鉄含有濾液5および塩化第二鉄
を主成分とするエツチング廃液(FeCl312.9%、
FeCl211.5%、CuCl25.1%)5を混合し、これ
に金属鉄を加えて残存する塩化第二鉄を塩化第一
鉄に、塩化第二銅を塩化第一銅にそれぞれ還元
し、沈澱を濾過したのち、粉末の塩化第一銅
700gを加え、第1表に記載の反応液を調整し、
該反応液中にアトマイズ鉄粉2.0Kgを投入し、鉄
粉表面に銅微粒子を付着させた銅被覆鉄粉2.2Kg
を得た。 実施例 6 塩化第二鉄を主成分とするエツチング廃液
(FeCl312.9%、FeCl211.5%、CuCl25.1%)10
に金属銅を用いて液中の塩化第二鉄、塩化第二銅
を塩化第一鉄、塩化第一銅にまで還元するととも
に沈澱を濾過して第1表に記載の反応液とし、該
反応液中にアトマイズ鉄粉2.1Kgを投入し、鉄粉
表面に銅微粒子を付着させた銅被覆鉄粉を得た。 実施例 7 鉄粉表面に銅微粒子を付着させる際に得た濃度
35%の塩化第一鉄含有濾液6.8中に塩化第二鉄
を主成分とするエツチング廃液(FeCl312.9%、
FeCl211.5%、CuCl25.1%)3.2を加え、金属銅
を用いて液中の塩化第二鉄、塩化第二銅を塩化第
一鉄、塩化第一銅にまで還元し、沈澱を濾過して
第1表に記載の反応液とし、該反応液中にアトマ
イズ鉄粉2.1Kgを投入し、鉄粉表面に銅微粒子を
付着させた銅被覆鉄粉を得た。 比較例 1 前記の各実施例で使用したアトマイズ決粉と同
じアトマイズ鉄粉2.0Kgを、濃度35%の塩化第二
銅溶液10中に投入して鉄粉表面に銅微粒子を被
覆した銅被覆鉄粉を得た。 以上の実施例1〜7および比較例1における反
応液の主要成分組成及び得られた製品の銅重量
(%)、見掛密度(g/cm2)、流動度(sec/50g)、
粒度分布(−350メツシユ)は、第1表のとおり
であつた。 なお、第1表において、各物性値はつぎの測定
方法に拠つた。 (1) 見掛密度(g/cm2);JIS Z 2504(金属粉の
見掛密度試験方法)に準拠し真鍮製漏斗(開角
60゜、オリフイス{φ=2.54mm、L=3.2mm}を
使用し、粉末を円筒容器(容量25±0.05c.c.)に
流し込み重量測定。 (2) 流動度(sec/50g);JIS Z 2502(金属粉の
流動度試験方法)に準拠し同上漏斗で粉末量
50gの流出時間を測定。 (3) 粒度分布−350(%);粉末量100g、自動篩機
で篩別、篩はTyler型で、350メツシユ篩下の
%を求めた。
[Industrial Application Field] The present invention relates to a method for producing copper-coated iron powder for powder metallurgy, which allows the surface of iron powder for powder metallurgy to be easily coated with copper. [Prior Art] Examples of forms conventionally used as materials for iron-copper sintered alloys for powder metallurgy include alloy powders and mixed powders. When alloy powder is used as a sintered alloy material, the particles are produced as iron-copper alloy powder by atomization, etc., so the particles have excellent uniformity, but the hardness of the particles is low. It has the disadvantage of poor moldability due to its high price. In addition, when mixed powder is used, uniform mixing is technically difficult, and the coarser the powder particles are, the more likely they are to cause polarization due to the influence of particle size and shape.
Moreover, the variation in sintered dimensions increases. In order to eliminate these drawbacks, various methods for producing copper-coated iron powder have been proposed. For example, there is a method in which iron powder for powder metallurgy is mixed with fine powder of metallic copper, copper oxide, or a reducing copper compound, and then heat treated in a reducing atmosphere to coat the surface of the iron powder with metallic copper fine particles. However, uniform mixing is required, and heat treatment progresses alloying of some of the coated particles, increasing the hardness of the particles, which adversely affects compressibility, formability, etc. In addition, it is difficult to select the particle size and mix balance between metallic copper, copper oxide, and reducing copper compound particles as copper raw materials and iron powder particles, and if the selection is inappropriate, iron particles and copper particles There is a risk that the adhesion of the product will be significantly reduced. There is also a wet method in which the surface of the iron powder is coated with metallic copper by immersing the iron powder in an aqueous solution of copper salts and displacing metallic iron and copper ions due to the difference in ionization tendency. Examples of aqueous solutions of copper salts include copper sulfate and cupric chloride. However, since the use of copper sulfate involves a chemical substitution reaction between divalent copper ions and metallic iron in a copper sulfate solution, a large amount of metallic iron is eluted into the aqueous solution as ferrous ions. Therefore, an amount of iron powder equivalent to the metal copper coated on the surface of the iron powder is lost, and the cost of the product increases by the amount of iron eluted. Another drawback is that the strength of the sintered body is significantly reduced by changing the shape of the iron powder due to the elution of metallic iron. Furthermore, when using cupric chloride solution,
Of course, the same problem as when using a copper sulfate solution can be considered, but instead of the surface of the iron powder being coated with uniform metallic copper fine particles, the copper is non-uniform and extends in the form of dendrites with poor adhesion. Because of the coating, the copper-coated iron powder produced by the conventional method has poor fluidity and cannot improve the formability, mechanical properties of the sintered body, etc. [Problems to be solved by the invention] Conventional technologies such as alloy powder, mixed powder, and copper-coated iron powder have their advantages and disadvantages, but especially regarding copper-coated iron powder, the above-mentioned copper sulfate and cupric chloride solutions are used. If the surface of the iron powder can be uniformly coated with metallic copper fine particles with less elution of metallic iron and good adhesion than in the case where iron powder is used, its usefulness as a powder metallurgy material can be increased. Moreover, if various etching waste liquids can be used as raw materials for copper to be coated while satisfying such conditions, cheaper materials for powder metallurgy can be obtained. This invention was completed as a result of research to address these problems. [Means for Solving the Problems] This invention uses iron powder for powder metallurgy such as atomized powder and reduced powder, and uses an etching waste liquid mainly composed of cupric chloride produced by etching metal materials; Alternatively, prepare a solution in which cuprous chloride is dissolved in a ferrous chloride solution and/or a sodium chloride solution made by reducing etching waste liquid containing ferric chloride as a main component, and add the powder metallurgy to this solution. In this method, the surface of the iron powder is uniformly coated with metallic copper fine particles by dipping the iron powder and using cuprous chloride as a raw material by a chemical substitution method. More specifically, metallic copper is added to an etching waste solution containing cupric chloride as a main component, and the cuprous chloride in which the cupric chloride is reduced is added to a ferrous chloride solution or/and sodium chloride. This method of producing copper-coated iron powder is characterized by immersing iron powder for powder metallurgy in a reaction solution dissolved in a solution, and coating the surface of the iron powder with metallic copper. In this invention, the raw material for the copper that is actually coated on the iron powder for powder metallurgy is cuprous chloride, and this cuprous chloride is a reaction solution obtained by dissolving it in a solution of ferrous chloride. be. Cuprous chloride, which is the copper raw material, has low solubility in water and is poorly soluble, so cuprous chloride alone cannot be used as a reaction solution by dispersing it in water. Therefore, we took advantage of the property of cuprous chloride to form and dissolve a complex salt in a solution containing a large amount of chlorine ions, such as a ferrous chloride solution or a sodium chloride solution, and used this as the reaction solution. The main purpose of this method is to suppress the formation of a dendrite-like coating of metallic copper that is uneven and has poor adhesion on the surface of iron powder, which occurs when a dicopper solution is used as the reaction solution. . Regarding such a suppressive effect, the proportion of dendrite-like copper deposits tends to increase as the concentration of ferrous chloride or sodium chloride decreases and as the reaction temperature increases. Therefore, for example, if a ferrous chloride solution containing cuprous chloride, which forms a complex salt, is used as the reaction solution, the concentration of ferrous chloride in the reaction solution should be set to 10% (wt%; the same applies hereinafter). The concentration of sodium chloride in the reaction solution is preferably 8% or more, especially 10% or more when a sodium chloride solution is used, and the reaction temperature is 60°C or less, especially 50% or more. It is desirable to carry out the test at temperatures below ℃. When the ferrous chloride and sodium chloride concentrations in the reaction solution are used in a dilute state below the above concentrations, or when the reaction temperature is too high, there is a tendency for dendrite-like metallic copper to adhere to the surface of the iron particles. Along with this, the apparent density and fluidity of the copper-coated iron powder also tend to decrease. Further, as the concentration of cuprous chloride, an appropriate concentration is selected so that the cuprous chloride forms a complex salt in the solution and dissolves. This is calculated from the target amount of copper deposited on the copper-coated iron powder, but on the other hand, it is also considered as the concentration required to form a copper coating by bringing the iron powder immersed in the reaction solution into contact with the solution under sufficient stirring. From these, either ferrous chloride solution or sodium chloride solution,
or cuprous chloride for solutions containing both.
A range of 0.5 to 10% can be said to be suitable. By adding iron powder into the reaction solution obtained as above while stirring it, or by adding the reaction solution into the iron powder and stirring for several tens of minutes, chemical Substitution reactions can be carried out. The iron powder coated with metallic copper is separated from the liquid after the substitution reaction has been completed, washed thoroughly with water until the remaining chlorine ions disappear, separated, and dried to obtain the desired copper-coated iron powder. I can do it. As the iron powder used in this invention, powdered metallic iron obtained by an atomization method, a reduction method, or other methods is used. There is no particular restriction on the particle size of these iron powders, and those having particle sizes that are conventionally used as iron powders for powder metallurgy are used. Here, regarding the amount of metallic copper to be coated on the surface of the iron powder, it is desirable to coat the copper coated iron powder to be a product in a range of 0.5 to 40%. If the above-mentioned coating amount is less than 0.5%, no improvement in the mechanical strength of the product as a sintered body can be expected;
If it exceeds %, the copper coating formed on the iron surface due to the copper substitution reaction becomes thicker, the elution of iron decreases accordingly, and the copper precipitation reaction tends to become less likely to occur, which is undesirable. Next, in the present invention, various etching waste liquids described below can be appropriately used as the reaction liquid. That is, when manufacturing copper printed wiring boards used as materials for electronic devices, etching is performed using an etching agent. As such an etching agent, an etching solution containing ferric chloride as a main component or an etching solution containing cupric chloride as a main component is used. Therefore, these waste liquids are inevitably produced during the manufacture of copper printed wiring boards. In addition, a solution containing ferric chloride as a main component is used as an etching solution for metal materials such as stainless steel, nickel, and cobalt, and as a matter of course, a waste solution is generated as the etching solution is used. The composition of metal compounds present in these waste liquids varies depending on the metal to be etched. For example, the waste liquid generated from an etching agent mainly composed of ferric chloride for copper printed wiring boards contains mainly ferric chloride as a metal compound, and also contains ferrous chloride and cupric chloride. ,
Even if the same etching agent is used for etching stainless steel, nickel, iron, etc., the cupric chloride will not be mixed in. Further, the waste liquid generated from an etching agent for copper printed wiring boards containing cupric chloride as a main component is a liquid that is almost exclusively composed of cupric chloride. This invention effectively utilizes the metal components in such waste liquid, and the main component is ferric chloride used in copper printed wiring boards. Copper is added to reduce the ferric chloride remaining in the solution to ferrous chloride and the cupric chloride to cuprous chloride, and these ferrous chloride and cuprous chloride are used. The reaction solution can be obtained by In addition, metal copper is added to the etching waste solution mainly composed of ferric chloride, which may or may not contain cupric chloride, to reduce the ferric chloride in the solution to ferrous chloride, and Produces cuprous metal,
It is possible to obtain a reaction solution using these methods, and it is also possible to obtain a reaction solution by using a combination of metallic iron and metallic copper depending on the composition of the waste solution. In addition, as mentioned above, metallic copper is added to the etching waste liquid mainly composed of cupric chloride generated by using an etching solution mainly composed of cupric chloride, and the remaining cupric chloride is removed by cuprous chloride. This can be dissolved in a ferrous chloride solution or a sodium chloride solution to obtain a reaction solution, and the iron powder for powder metallurgy is immersed in the reaction solution thus obtained as described above. Copper-coated iron powder can be produced. Furthermore, in the present invention, when immersing iron powder for powder metallurgy in a reaction liquid and forming a coating of metallic copper on the surface of the iron powder for powder metallurgy, the copper-coated iron powder is filtered from the reaction liquid. The ferrous chloride solution in the filtrate can be combined with the etching solution to effectively reuse the ferrous chloride in the filtrate, thereby producing copper-coated iron powder at low cost. be able to. In addition, since the use of a ferrous chloride-containing filtrate causes accumulation of ferrous chloride within the circulation system, it is desirable to carry out the test while drawing a portion of the filtrate out of the system. [Function] The method of the present invention uses various etching waste solutions to form metallic copper on the surface of iron powder using a reaction solution obtained by dissolving the obtained cuprous chloride in a ferrous chloride solution and/or a sodium chloride solution. However, cuprous chloride, which is originally poorly soluble, forms a complex salt in ferrous chloride solution and/or sodium chloride solution and becomes soluble, and due to the difference in ionization tendency, iron powder A uniform coating of metallic copper can be formed on the surface. [Examples] The present invention will be described in detail below with reference to Examples and Comparative Examples. Example 1 Metallic copper is added to 1.5 liters of etching waste solution (CuCl 2 24.0%) containing cupric chloride as the main component to reduce cupric chloride to cuprous chloride, which is then converted into cuprous chloride with a concentration of 35%. The reaction mixture was added to 8.5 ml of iron solution and stirred, and the precipitate was filtered to prepare the reaction solution shown in Table 1. Next, 1.9 kg of atomized iron powder was added to the reaction solution, and copper fine particles were attached to the surface of the iron powder to obtain 2.1 kg of copper-coated iron powder. Example 2 Metallic copper was added to 1.5 liters of etching waste solution (CuCl 2 24.0%) containing cupric chloride as the main component to reduce cupric chloride to cuprous chloride, which was then converted into a sodium chloride solution with a concentration of 28%. After stirring and filtering the precipitate, the reaction solution was prepared as shown in Table 1. Next, 1.9 kg of atomized iron powder was added to the reaction solution, and copper fine particles were attached to the surface of the iron powder to obtain 2.1 kg of copper-coated iron powder. Example 3 Concentration obtained when depositing copper fine particles on the surface of iron powder
Etching waste liquid mainly composed of cupric chloride (CuCl 2 24.0%) in filtrate 8.5% containing 35% ferrous chloride
1.5, further reduce the cupric chloride in the liquid to cuprous chloride using metallic copper, filter it and
Obtain the reaction solution shown in the table, and add atomized iron powder to this reaction solution.
1.9 kg of iron powder was added, and copper fine particles were attached to the surface of the iron powder to obtain 2.0 kg of copper-coated iron powder. Example 4 Etching waste liquid mainly composed of ferric chloride (FeCl 3 12.9%, FeCl 2 11.5%, CuCl 2 5.1%) 10
Metallic iron is added to reduce the remaining ferric chloride to ferrous chloride and cupric chloride to cuprous chloride, and after filtering the precipitate, powdered cuprous chloride is obtained.
700g was added to prepare the reaction solution shown in Table 1. Next, 2.0 kg of atomized iron powder was added to the reaction solution, and copper fine particles were attached to the surface of the iron powder to obtain 2.2 kg of copper-coated iron powder. Example 5 Concentration obtained when depositing copper fine particles on the surface of iron powder
Filtrate 5 containing 35% ferrous chloride and etching waste liquid mainly composed of ferric chloride (FeCl 3 12.9%,
FeCl 2 11.5%, CuCl 2 5.1%) 5 are mixed, metallic iron is added to this to reduce the remaining ferric chloride to ferrous chloride, cupric chloride to cuprous chloride, and precipitate. After filtering, powdered cuprous chloride
Add 700g and prepare the reaction solution listed in Table 1.
2.0 kg of atomized iron powder was added to the reaction solution, and 2.2 kg of copper-coated iron powder was prepared by adhering fine copper particles to the surface of the iron powder.
I got it. Example 6 Etching waste liquid mainly composed of ferric chloride (FeCl 3 12.9%, FeCl 2 11.5%, CuCl 2 5.1%) 10
The ferric chloride and cupric chloride in the solution are reduced to ferrous chloride and cuprous chloride using metallic copper, and the precipitate is filtered to obtain the reaction solution listed in Table 1. 2.1 kg of atomized iron powder was put into the liquid to obtain copper-coated iron powder with copper fine particles attached to the surface of the iron powder. Example 7 Concentration obtained when depositing copper fine particles on the surface of iron powder
Etching waste solution mainly composed of ferric chloride (FeCl 3 12.9%,
Add FeCl 2 11.5%, CuCl 2 5.1%) 3.2, reduce the ferric chloride and cupric chloride in the solution to ferrous chloride and cuprous chloride using metallic copper, and filter the precipitate. A reaction solution as shown in Table 1 was prepared, and 2.1 kg of atomized iron powder was added to the reaction solution to obtain copper-coated iron powder with fine copper particles attached to the surface of the iron powder. Comparative Example 1 2.0 kg of atomized iron powder, which is the same as the atomized final powder used in each of the above examples, was put into a cupric chloride solution with a concentration of 35% to coat copper fine particles on the surface of the iron powder to produce copper-coated iron. Got the powder. The main component composition of the reaction solution in Examples 1 to 7 and Comparative Example 1 and the copper weight (%), apparent density (g/cm 2 ), fluidity (sec/50g) of the obtained product,
The particle size distribution (-350 mesh) was as shown in Table 1. In addition, in Table 1, each physical property value was based on the following measurement method. (1) Apparent density (g/cm 2 ): Based on JIS Z 2504 (Metal powder apparent density test method), a brass funnel (opening angle
Using a 60° orifice {φ=2.54mm, L=3.2mm}, pour the powder into a cylindrical container (capacity 25±0.05cc) and measure its weight. (2) Fluidity (sec/50g): Measure the amount of powder using the same funnel in accordance with JIS Z 2502 (metal powder fluidity test method).
Measure the outflow time of 50g. (3) Particle size distribution -350 (%); Powder amount: 100 g, sieved using an automatic sieve machine, the sieve was a Tyler type sieve, and the % below the 350 mesh sieve was determined.

【表】 参考例 1〜7 実施例1〜7および比較例1で得た銅被覆鉄粉
にアトマイズ鉄粉を所定量添加し、また黒鉛粉末
0.5%、ステアリン酸亜鉛0.75%を添加し、各配
合比として、Fe−1.5・Cu−0.5・C−0.5・Znst
としたものを用いて、成形圧力7.0t/cm2で直径
18m/mのタブレツト各3個作製し、圧粉密度
(g/cm2)ラトラー値(%)、燒結体寸法変化率
(%)を測定した。これを第2表に示す。 なお、第2表において、各物性値はつぎの測定
方法に拠つた。 (1) 圧粉密度(g/cm2);JSPM標準1−64(金属
粉の圧縮性試験法)により、一定の条件下で金
属粉を押型中で圧縮し、加圧終了後圧粉体を押
型から抜き出して、次式により算出した圧粉体
の密度である。 P=W/0.785×D2×H P;圧粉密度(g/cm2) D;圧粉体の直径(cm) W;圧粉体の重量(g) H;圧粉体の高さ(cm) (2) ラトラー値;JSPM標準4−64(金属圧粉体
のラトラー試験法)により加圧成形した金属圧
粉体の耐摩耗性及び先端安定性を測定する。装
置としてはフルイ目1190μをもつ青銅製網を張
つた円筒型の籠と、この籠を駆動回転するため
の電動機並びに試験回転を表示する試験回転表
示装置よりなる。 試験方法としては同一圧力で成形した試験片
を5個まとめて0.01/gのケタまで計つたの
ち、籠の中に入れ、87±10rpmの速さで1000回
転後取り出し5個まとめて0.01/gケタまで計
る。金属粉体のラトラー試験の結果は次式によ
つて算出される。 S=A−B/A×100(%) S;重量減少率(%) A;試験片の試験前の重量(g) B:試験片の試験後の重量(g) (3) 燒結体寸法変化率(%);燒結の際の収縮あ
るい膨張による寸法の変化を燒結前の寸法に対
する百分率で表したものである。 なお、表中の参考例の番号は実施例の番号に
対応するものである。
[Table] Reference Examples 1 to 7 A specified amount of atomized iron powder was added to the copper-coated iron powder obtained in Examples 1 to 7 and Comparative Example 1, and graphite powder was added to the copper-coated iron powder obtained in Examples 1 to 7 and Comparative Example 1.
0.5%, zinc stearate 0.75%, each blending ratio is Fe-1.5, Cu-0.5, C-0.5, Znst.
diameter at a molding pressure of 7.0t/ cm2 .
Three tablets of 18 m/m each were prepared, and the green density (g/cm 2 ), Rattler value (%), and sintered body dimensional change rate (%) were measured. This is shown in Table 2. In addition, in Table 2, each physical property value was based on the following measurement method. (1) Green powder density (g/cm 2 ): According to JSPM Standard 1-64 (compressibility test method for metal powder), metal powder is compressed in a die under certain conditions, and after the compression is finished, the green powder is This is the density of the green compact calculated by the following formula after being extracted from the mold. P=W/0.785×D 2 ×H P: Green density (g/cm 2 ) D: Diameter of green compact (cm) W: Weight of green compact (g) H: Height of green compact ( cm) (2) Rattler value: Measures the wear resistance and tip stability of a pressure-formed metal compact according to JSPM Standard 4-64 (Rattler test method for metal compacts). The device consists of a cylindrical cage covered with a bronze mesh with a mesh size of 1190μ, an electric motor to drive and rotate the cage, and a test rotation display device to display the test rotation. The test method is to measure 5 test pieces molded at the same pressure to the nearest 0.01/g, then place them in a basket and after 1000 rotations at a speed of 87±10 rpm, take out the 5 test pieces and weigh them to the nearest 0.01/g. Measure to the nearest digit. The results of the Rattler test for metal powder are calculated using the following formula. S=A-B/A×100 (%) S: Weight reduction rate (%) A: Weight of test piece before test (g) B: Weight of test piece after test (g) (3) Sintered body size Change rate (%): Change in dimension due to contraction or expansion during sintering, expressed as a percentage of the dimension before sintering. Note that the numbers of reference examples in the table correspond to the numbers of examples.

【表】【table】

〔発明の効果〕〔Effect of the invention〕

この発明は、各種エツチング廃液より塩化第一
鉄溶液又は/及び食塩溶液中に塩化第一銅を溶解
せしめた液を取得し、これを使用して鉄粉表面に
銅被覆を施すことによつて鉄粉の溶出が少なく、
しかも銅の付着性に優れた銅被覆鉄粉を容易かつ
きわめて廉価に得ることができ、かゝかる発明に
より得た製品を使用することにより圧縮性、成形
性及び機械的性質等の各種の特性に優れた機械部
品を得ることができる。 また、この発明においては、粉末冶金用鉄粉の
表面を金属銅で被覆する際に得られる塩化第一銅
含有濾液を、エツチング廃液と合流せしめて塩化
第一鉄溶液として再度使用することによつて塩化
第一鉄の有効利用を図ることができ、より一層安
価な銅被覆鉄粉を収得しうるものである。
This invention obtains a liquid in which cuprous chloride is dissolved in a ferrous chloride solution and/or a salt solution from various etching waste liquids, and uses this to coat the surface of iron powder with copper. Less elution of iron powder,
Moreover, copper-coated iron powder with excellent copper adhesion can be obtained easily and at a very low cost, and by using the product obtained by such invention, various properties such as compressibility, formability, and mechanical properties can be obtained. You can obtain excellent mechanical parts. Furthermore, in this invention, the cuprous chloride-containing filtrate obtained when coating the surface of powder metallurgy iron powder with metallic copper is combined with the etching waste liquid and reused as a ferrous chloride solution. Therefore, ferrous chloride can be used effectively, and copper-coated iron powder can be obtained at a lower cost.

Claims (1)

【特許請求の範囲】 1 塩化第二銅を主成分とするエツチング廃液に
金属銅を加えてその中の塩化第二銅を還元せしめ
た塩化第一銅を、塩化第一鉄溶液又は/及び塩化
ナトリウム溶液に溶解せしめてなる反応液に、粉
末冶金用鉄粉を浸漬し、該鉄粉の表面を金属銅に
より被覆することを特徴とする銅被覆鉄粉の製
法。 2 前記粉末冶金用鉄粉の表面を金属銅で被覆す
るに際に得られた塩化第一鉄含有濾液を、前記塩
化第一鉄溶液の一部もしくは全部として使用する
ことを特徴とする特許請求の範囲第1項記載の銅
被覆鉄粉の製法。 3 塩化第二鉄を主成分とするエツチング廃液に
金属鉄を加え、その中の塩化第二鉄を還元せしめ
て得られる塩化第一鉄溶液中に塩化第一銅を溶解
して得た反応液に、粉末冶金用鉄粉を浸漬し、該
粉末冶金用鉄粉の表面を金属銅により被覆するこ
とを特徴とする銅被覆鉄粉の製法。 4 塩化第二鉄を主成分とするエツチング廃液に
金属鉄を加え、その中の塩化第二鉄を還元せしめ
て得られる塩化第一鉄溶液中に塩化第一銅を溶解
して得た反応液に、粉末冶金用鉄粉を浸漬し、該
粉末冶金用鉄粉の表面を金属銅により被覆するこ
とからなり、前記粉末冶金用鉄粉の表面を金属銅
で被覆する際に得られた塩化第一鉄含有濾液を、
前記エツチング廃液に混合して使用することを特
徴とする銅被覆鉄粉の製法。 5 塩化第二鉄を主成分とするエツチング廃液に
金属銅を加えて該塩化第二鉄の還元による塩化第
一鉄の生成および塩化第一銅の生成を行わしめ、
得たる塩化第一鉄の塩化第一銅溶解反応液に、粉
末冶金用鉄粉を浸漬し、該粉末冶金用鉄粉の表面
を金属銅により被覆することを特徴とする銅被覆
鉄粉の製法。 6 塩化第二鉄を主成分とするエツチング廃液に
金属銅を加えて該塩化第二鉄の還元による塩化第
一鉄の生成および塩化第一銅の生成を行わしめ、
得たる塩化第一鉄の塩化第一銅溶解反応液に、粉
末冶金用鉄粉を浸漬し、該粉末冶金用鉄粉の表面
を金属銅により被覆することからなり、前記粉末
冶金用鉄粉の表面を金属銅で被覆する際に得られ
た塩化第一鉄含有濾液を前記エツチング廃液に混
合して使用することを特徴とする銅被覆鉄粉の製
法。
[Scope of Claims] 1 Cuprous chloride, which is obtained by adding metallic copper to an etching waste solution containing cupric chloride as a main component to reduce the cupric chloride therein, is added to a ferrous chloride solution or/and chloride. A method for producing copper-coated iron powder, which comprises immersing iron powder for powder metallurgy in a reaction solution dissolved in a sodium solution, and coating the surface of the iron powder with metallic copper. 2. A patent claim characterized in that the ferrous chloride-containing filtrate obtained when the surface of the iron powder for powder metallurgy is coated with metallic copper is used as part or all of the ferrous chloride solution. A method for producing copper-coated iron powder according to item 1. 3. A reaction solution obtained by dissolving cuprous chloride in a ferrous chloride solution obtained by adding metallic iron to an etching waste solution containing ferric chloride as a main component and reducing the ferric chloride therein. 1. A method for producing copper-coated iron powder, which comprises immersing iron powder for powder metallurgy in a method, and coating the surface of the iron powder for powder metallurgy with metallic copper. 4. A reaction solution obtained by dissolving cuprous chloride in a ferrous chloride solution obtained by adding metallic iron to an etching waste solution containing ferric chloride as a main component and reducing the ferric chloride therein. The iron powder for powder metallurgy is immersed in the powder metallurgy, and the surface of the iron powder for powder metallurgy is coated with metallic copper. The iron-containing filtrate,
A method for producing copper-coated iron powder, characterized in that the copper-coated iron powder is used by mixing it with the etching waste solution. 5. Adding metallic copper to an etching waste solution containing ferric chloride as a main component to reduce the ferric chloride to produce ferrous chloride and cuprous chloride,
A method for producing copper-coated iron powder, which comprises immersing iron powder for powder metallurgy in the obtained cuprous chloride dissolution reaction solution of ferrous chloride, and coating the surface of the iron powder for powder metallurgy with metallic copper. . 6. Adding metallic copper to an etching waste solution containing ferric chloride as a main component to reduce the ferric chloride to generate ferrous chloride and cuprous chloride,
The process consists of immersing iron powder for powder metallurgy in the obtained cuprous chloride dissolution reaction solution of ferrous chloride, and coating the surface of the iron powder for powder metallurgy with metallic copper. A method for producing copper-coated iron powder, characterized in that a ferrous chloride-containing filtrate obtained when the surface is coated with metallic copper is mixed with the etching waste solution.
JP59202185A 1984-09-27 1984-09-27 Production of copper-coated iron powder Granted JPS6179707A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59202185A JPS6179707A (en) 1984-09-27 1984-09-27 Production of copper-coated iron powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59202185A JPS6179707A (en) 1984-09-27 1984-09-27 Production of copper-coated iron powder

Publications (2)

Publication Number Publication Date
JPS6179707A JPS6179707A (en) 1986-04-23
JPH058242B2 true JPH058242B2 (en) 1993-02-01

Family

ID=16453370

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59202185A Granted JPS6179707A (en) 1984-09-27 1984-09-27 Production of copper-coated iron powder

Country Status (1)

Country Link
JP (1) JPS6179707A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4833040A (en) * 1987-04-20 1989-05-23 Trw Inc. Oxidation resistant fine metal powder
US4975333A (en) * 1989-03-15 1990-12-04 Hoeganaes Corporation Metal coatings on metal powders
US5240742A (en) * 1991-03-25 1993-08-31 Hoeganaes Corporation Method of producing metal coatings on metal powders
CN101534980B (en) * 2006-11-17 2012-06-13 Jx日矿日石金属株式会社 Iron/copper composite powder for powder metallurgy and process for producing the same
JP6493679B2 (en) * 2015-08-25 2019-04-03 東亞合成株式会社 Copper powder recovery method
CN108311692A (en) * 2018-05-03 2018-07-24 佛山九陌科技信息咨询有限公司 A kind of preparation method at anti-oxidant copper-coated iron composite powder end
CN111451519B (en) * 2020-04-03 2022-10-14 龙门金南磁性材料有限公司 Preparation method of brass-coated iron powder

Also Published As

Publication number Publication date
JPS6179707A (en) 1986-04-23

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