JPS6149369B2 - - Google Patents

Info

Publication number
JPS6149369B2
JPS6149369B2 JP130884A JP130884A JPS6149369B2 JP S6149369 B2 JPS6149369 B2 JP S6149369B2 JP 130884 A JP130884 A JP 130884A JP 130884 A JP130884 A JP 130884A JP S6149369 B2 JPS6149369 B2 JP S6149369B2
Authority
JP
Japan
Prior art keywords
copper
copper oxide
oxide powder
molten
molten copper
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
Application number
JP130884A
Other languages
Japanese (ja)
Other versions
JPS60145336A (en
Inventor
Minoru Konuma
Masao Yamauchi
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric 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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Priority to JP130884A priority Critical patent/JPS60145336A/en
Publication of JPS60145336A publication Critical patent/JPS60145336A/en
Publication of JPS6149369B2 publication Critical patent/JPS6149369B2/ja
Granted legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】 本発明は酸化銅粉から銅を回収する方法並にそ
の装置の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to improvements in a method and apparatus for recovering copper from copper oxide powder.

従来酸化銅粉は乾燥した後、再溶解せしめ溶湯
状態において、これを還元しなるべく酸化成分の
低い酸化銅とした後、純銅と混合してアノードと
して使用しているものである。然しながらこの方
法は乾燥工程、溶解工程及び還元工程の如く複雑
な処理によるものであると共に莫大なエネルギー
を必要とするためコストが高くなるものであつ
た。
Conventionally, copper oxide powder is dried, then remelted and reduced in a molten state to copper oxide with as low an oxidizing component as possible, which is then mixed with pure copper and used as an anode. However, this method requires complicated processing such as a drying step, a dissolution step, and a reduction step, and requires a huge amount of energy, resulting in high costs.

なお上記の酸化銅は銅製品の製造工程と一貫し
て連続的に操業することなく別工場又は別工程に
より行われているものである。
Note that the above-mentioned copper oxide is produced in a separate factory or in a separate process without being operated continuously and consistently with the manufacturing process of copper products.

本発明はかかる現状に鑑み鋭意研究を行つた結
果、酸化銅粉を連続工程によつて短時間に銅製品
用銅として回収する方法及び装置を提供せんとす
るものである。即ち本発明の回収方法は酸化銅供
給口及び還元炎用噴出口を取付けた還元炉の該酸
化銅供給口から酸化銅粉を投入しつつ該還元炎用
噴出口から常圧又は加圧の還元性フレームを該酸
化銅粉に吹付けて該酸化銅粉の表皮を還元すると
共に溶融せしめて還元溶銅となした後、該還元炉
に直結し且つシヤフト炉により溶解した高純度溶
銅を導入せる溶銅樋内に上記還元溶銅を併流せし
めて混合し、鋳造装置により鋳造することを特徴
とするものである。
As a result of extensive research in view of the current situation, the present invention aims to provide a method and apparatus for recovering copper oxide powder as copper for copper products in a short period of time through a continuous process. That is, the recovery method of the present invention is to introduce copper oxide powder from the copper oxide supply port of a reduction furnace equipped with a copper oxide supply port and a reduction flame jet port, and perform reduction under normal pressure or pressurization from the reduction flame jet port. After spraying the copper oxide powder onto the copper oxide powder to reduce the skin of the copper oxide powder and melting it to form reduced molten copper, the high-purity molten copper directly connected to the reduction furnace and melted by a shaft furnace is introduced. The method is characterized in that the reduced molten copper is made to flow together in a molten copper gutter, mixed, and then cast by a casting device.

又回収装置としては一端に酸化銅粉を投入する
酸化銅供給口と、還元性フレームを噴出せしめる
還元炎用噴出口とを、該還元性フレームにて酸化
銅粉を加熱し溶融しうる位置に設けた還元炉の他
端に予めシヤフト炉によりえた高純度溶銅を導入
せしめる溶銅流入口を設けた溶銅樋を取付けたこ
とを特徴とするものである。
In addition, the recovery device has a copper oxide supply port for introducing copper oxide powder into one end, and a reducing flame jet port for spouting a reducing flame at a position where the reducing flame can heat and melt the copper oxide powder. The present invention is characterized in that a molten copper gutter is attached to the other end of the reduction furnace provided with a molten copper inlet into which high-purity molten copper previously produced by a shaft furnace is introduced.

本発明方法において酸化銅粉の品質については
特に限定するものではないが、酸化銅粉中に酸素
量が多いもの例えば酸素量が15%程度含有せるも
のはタフピツチ銅に還元し難く、酸素量の少いも
の例えば酸素量が3000ppm程度含有せるものは
ほとんどタフピツチ銅に近く還元されるものであ
る。なお酸化銅粉の粒度については細粉化するこ
とにより還元効率が向上する。
In the method of the present invention, there are no particular limitations on the quality of the copper oxide powder, but if the copper oxide powder contains a large amount of oxygen, for example, one containing about 15% oxygen, it will be difficult to reduce it to tough copper, and the amount of oxygen will decrease. Those containing a small amount of oxygen, for example, around 3000 ppm, are almost reduced to tough copper. Regarding the particle size of the copper oxide powder, the reduction efficiency is improved by making it finer.

又本発明方法における還元性フレームとして
は、ガス体例えばLPGと空気との混合ガスを使用
するものである。この還元性フレームは常圧でも
よいが、加圧状態例えば0.05〜0.1Kg/cm2程度に
して酸化銅粉に吹付けることにより、この両者が
還元炉内にて撹乱し還元性フレームと酸化銅粉と
は均一化され酸化銅粉の表皮を効率よく且つ十分
に還元せしめることが出来る。
Further, as the reducing flame in the method of the present invention, a gaseous material such as a mixed gas of LPG and air is used. This reducible flame may be under normal pressure, but by spraying it onto the copper oxide powder at a pressurized state of, for example, 0.05 to 0.1 Kg/cm 2 , both of them are disturbed in the reduction furnace, and the reducible flame and the copper oxide powder are sprayed together. The powder is homogenized and the skin of the copper oxide powder can be efficiently and sufficiently reduced.

又本発明方法において溶銅樋内に還元炉にて還
元された溶銅(還元溶銅という)とシヤフト炉に
より溶融せしめた高純度溶銅とを併流せしめる理
由は、酸化銅粉を還元するも上記の如く高純度銅
をうることが出来難いため、この還元溶銅のみで
は鋳造するも銅製品として使用出来難い場合、そ
の目的に応じて高純度溶銅中に所定量の還元溶銅
を混合して使用するためである。
In addition, in the method of the present invention, the reason why molten copper reduced in a reduction furnace (referred to as reduced molten copper) and high-purity molten copper melted in a shaft furnace are made to flow together in the molten copper gutter is to reduce the oxidized copper powder. As mentioned above, it is difficult to obtain high-purity copper, so if this reduced molten copper alone cannot be used as a copper product even though it is cast, a predetermined amount of reduced molten copper may be mixed into the high-purity molten copper depending on the purpose. This is for the purpose of use.

次に本発明方法の実施例を図面の装置により説
明する。
Next, an embodiment of the method of the present invention will be explained using the apparatus shown in the drawings.

実施例 一端に還元用フレーム3を噴出する還元炎用噴
出口2を取付け、この近傍に該フレームに直交し
てホツパ5酸化銅粉6を投入する酸化銅供給口4
を設けた円筒状還元炉1を該噴出口2が高くなる
ように傾斜せしめ、その他端に溶銅樋7を取付け
る。この溶銅樋7にはシヤフト炉(図示せず)に
よりえた高純度溶銅8を導入せしめるための溶銅
流入口9を設けているものである。
Embodiment A reducing flame spout 2 for spouting out a reducing flame 3 is attached to one end, and a copper oxide supply port 4 for feeding a hopper 5 and copper oxide powder 6 in a direction perpendicular to the frame near this
A cylindrical reduction furnace 1 provided with a cylindrical reduction furnace 1 is tilted so that the spout 2 is raised, and a molten copper gutter 7 is attached to the other end. This molten copper gutter 7 is provided with a molten copper inlet 9 for introducing high purity molten copper 8 produced by a shaft furnace (not shown).

而して酸化銅供給口2にホツパ5を取付け、該
ホツパ内に酸化銅粉(酸素量7000ppm、平均粒
度500ミクロン)5を充填し、還元炉1内に1.5〜
2.0Kg/minの条件にて投入する。一方ブタンガ
スと空気との混合ガスフレーム3を混合ガス中の
水素1.5〜2.5%の条件にて噴出せしめて該酸化銅
粉5に吹付けた。
Then, a hopper 5 is attached to the copper oxide supply port 2, and copper oxide powder (oxygen content 7000 ppm, average particle size 500 microns) 5 is filled into the hopper, and 1.5~
Input under the condition of 2.0Kg/min. On the other hand, a mixed gas flame 3 of butane gas and air was ejected under conditions of 1.5 to 2.5% hydrogen in the mixed gas and sprayed onto the copper oxide powder 5.

なおフレームと酸化銅粉とは約30cm程度離間せ
しめているものである。
Note that the frame and the copper oxide powder are separated by about 30 cm.

酸化銅粉はガスフレームによつて約1200℃程度
となり、その表皮は還元されつつ溶融し、該還元
炉の内壁を伝つて降下し溶銅樋へと流出する。又
別にシヤフト炉(図示せず)によりえた高純度の
溶銅8を溶銅流入口9から溶銅樋7内に流入せし
め、上記の還元溶銅と混合し、この混合溶銅を鋳
造装置に送り鋳造して銅インゴツトをうるもので
ある。
The copper oxide powder is heated to about 1200°C by the gas flame, and its skin is reduced and melted, descending along the inner wall of the reduction furnace and flowing out into the molten copper gutter. Separately, high-purity molten copper 8 obtained from a shaft furnace (not shown) is made to flow into the molten copper gutter 7 from the molten copper inlet 9, mixed with the above-mentioned reduced molten copper, and this mixed molten copper is sent to the casting machine. Copper ingots are obtained by feed casting.

斯くして本発明方法によりえた銅インゴツトに
ついてその酸素量を測定した結果、500〜
700ppmであり、著しく酸素量が減少し純銅化し
ていることを示した。
As a result of measuring the oxygen content of the copper ingot obtained by the method of the present invention, it was found that it was 500~
It was 700ppm, indicating that the amount of oxygen was significantly reduced and the content was pure copper.

以上詳述した如く本発明によれば簡単な工程並
に低エネルギによつて酸化銅粉より銅を効率よく
回収しうると共に鋳造等の後工程の操業を連続し
て行いうる等顕著な効果を有する。
As detailed above, according to the present invention, it is possible to efficiently recover copper from copper oxide powder through simple steps and low energy consumption, and it also has remarkable effects such as being able to continuously operate post-processes such as casting. have

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

図面は本発明において銅を回収するための装置
の1例を示す概略説明図である。 1……還元炉、2……還元性フレーム供給口、
3……還元性フレーム、4……酸化銅粉供給口、
6……酸化銅粉、7……溶銅樋。
The drawing is a schematic explanatory diagram showing one example of an apparatus for recovering copper in the present invention. 1... Reduction furnace, 2... Reducing frame supply port,
3... Reducing frame, 4... Copper oxide powder supply port,
6... Oxidized copper powder, 7... Molten copper gutter.

Claims (1)

【特許請求の範囲】 1 酸化銅供給口及び還元炎用噴出口を取付けた
還元炉の該酸化銅供給口から酸化銅粉を投入しつ
つ、該還元炎用噴出口から常圧又は加圧せる還元
性フレームを該酸化銅粉に吹付けて該酸化銅粉の
表皮を還元すると共に溶融せしめて還元溶銅とな
した後、該還元炉に直結し且つシヤフト炉により
溶融せしめた高純度溶銅を導入せる溶銅樋内に上
記還元溶銅を併流せしめて混合し、鋳造装置によ
り鋳造することを特徴とする銅の回収方法。 2 一端に酸化銅粉を投入する酸化銅供給口と、
還元性フレームを噴出せしめる還元炎用噴出口と
を、該還元性フレームにて酸化銅粉を加熱し溶融
しうる位置に設けた還元炉の他端に予めシヤフト
炉によりえた高純度溶銅を導入せしめる溶銅流入
口を設けた溶銅樋を取付けたことを特徴とする銅
の回収装置。
[Scope of Claims] 1. While introducing copper oxide powder from the copper oxide supply port of a reducing furnace equipped with a copper oxide supply port and a reducing flame jet port, normal pressure or pressurization can be carried out from the reducing flame jet port. High-purity molten copper that is directly connected to the reduction furnace and melted in a shaft furnace after spraying a reducing flame onto the copper oxide powder to reduce the skin of the copper oxide powder and melting it to form reduced molten copper. A method for recovering copper, characterized in that the reduced molten copper is co-flowed into a molten copper gutter into which the molten copper is introduced, mixed, and then cast using a casting device. 2. A copper oxide supply port into which copper oxide powder is introduced at one end;
High-purity molten copper prepared in advance by a shaft furnace is introduced into the other end of the reducing furnace, in which a reducing flame spout for ejecting a reducing flame is installed at a position where the reducing flame can heat and melt the copper oxide powder. A copper recovery device characterized by being equipped with a molten copper gutter having a molten copper inlet.
JP130884A 1984-01-10 1984-01-10 Method and device for recovering copper Granted JPS60145336A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP130884A JPS60145336A (en) 1984-01-10 1984-01-10 Method and device for recovering copper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP130884A JPS60145336A (en) 1984-01-10 1984-01-10 Method and device for recovering copper

Publications (2)

Publication Number Publication Date
JPS60145336A JPS60145336A (en) 1985-07-31
JPS6149369B2 true JPS6149369B2 (en) 1986-10-29

Family

ID=11497861

Family Applications (1)

Application Number Title Priority Date Filing Date
JP130884A Granted JPS60145336A (en) 1984-01-10 1984-01-10 Method and device for recovering copper

Country Status (1)

Country Link
JP (1) JPS60145336A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200228495Y1 (en) * 2001-01-19 2001-06-15 유영수 apparatus of the copper from waste cables

Also Published As

Publication number Publication date
JPS60145336A (en) 1985-07-31

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