JPS6220841A - Treatment of copper converter slag - Google Patents
Treatment of copper converter slagInfo
- Publication number
- JPS6220841A JPS6220841A JP15941685A JP15941685A JPS6220841A JP S6220841 A JPS6220841 A JP S6220841A JP 15941685 A JP15941685 A JP 15941685A JP 15941685 A JP15941685 A JP 15941685A JP S6220841 A JPS6220841 A JP S6220841A
- Authority
- JP
- Japan
- Prior art keywords
- melt
- converter
- matte
- slag
- 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.)
- Pending
Links
Abstract
Description
【発明の詳細な説明】
(イ)技術分野
本発明は、銅製錬工程で発生する転炉跡中に混入した鎖
を効率よく分離回収する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (a) Technical Field The present invention relates to a method for efficiently separating and recovering chains mixed in the remains of a converter generated in a copper smelting process.
(ロ)従来技術
CuFe5 y等の硫化物である銅精鉱は、一般に自溶
炉、溶鉱炉9反射炉等で溶練されてFeS −Cu7
S系の鋳となり、更に転炉で粗銅となるが。(b) Prior art Copper concentrate, which is a sulfide such as CuFe5y, is generally smelted in a flash furnace, blast furnace 9 reverberatory furnace, etc.
It becomes S-type casting and then becomes blister copper in a converter.
この際転炉で生成され排出されるFeO−5iO2系の
転炉↑男(からみ)中には金、銀、銅、鎖環有価金属の
濃縮物である鶏(かわ)が含有されている。At this time, the FeO-5iO2-based converter ↑ man produced and discharged from the converter contains gold, silver, copper, and Kawa, which is a concentrate of chain and ring valuable metals.
しかるに、従来この転炉r1の処理法としては、a)転
炉跡をスラグコンベヤにて運搬冷却固化して粉砕後、浮
遊選鉱により転炉n中に混入した訪を分離回収する方法
(このフローを第1図に示す)や、
b)転炉3Aを溶体のまま溶錬炉、セットリング炉等へ
僅返しコークス等を添加して転炉鋳の溶体1−に浮遊さ
せ、溶体表面の酸化・固化を防1ヒしながら転炉訪中の
鎖と拐とを相17.分離させる方法(このフローを第2
図に示す)等があるが、1−記a法は選鉱工程の介在に
より製錬コストが高くなり、また他方ヒ記す法において
は転炉跡がマグネタイトを飽和又は飽和に近く含有して
いるため、流動度が悪くて鶏と斜の分離性が悪化し、有
価金属の実収率が非常に低く効率も悪いなどの欠点があ
った。However, conventional methods for treating this converter r1 include a) a method in which the remains of the converter are transported on a slag conveyor, cooled, solidified, and pulverized, and the slag mixed into the converter n is separated and recovered by flotation; (shown in Figure 1), or b) The converter 3A is transferred to a smelting furnace, settling furnace, etc. as a melt, and a small amount of coke, etc. is added and suspended in the melt 1- of the converter casting to oxidize the surface of the melt.・While preventing solidification, the chains and wires of the converter are 17. Separation method (this flow is used in the second
However, in method 1-a, the smelting cost is high due to the intervention of the beneficiation process, and on the other hand, in the method described in (h), the remains of the converter contain magnetite at or near saturation. However, there were drawbacks such as poor fluidity, poor separation of the sludge, and very low yield of valuable metals and low efficiency.
(ハ)発明の開示及び実施例
本発明は、溶体状の銅転炉錫をセットリング炉へ装入し
た後、微粉炭等の還元剤を該溶体内へ羽目からあるいは
ランス等により吹込んでマグネタイトを還元することに
より、該溶体の流動性を向にさせて鎖と錫との相互分離
を促進させるものである。(c) Disclosure and Examples of the Invention The present invention involves charging tin in a copper converter in a solution state into a settling furnace, and then injecting a reducing agent such as pulverized coal into the solution through a slat or with a lance to produce magnetite. By reducing , the fluidity of the solution is improved and the mutual separation of the chains and tin is promoted.
回収された鋳は、溶錬炉にて生成された鋳とノ(に転炉
で酸化処理し、粗銅を得る。このフローを第3図に示す
。The recovered cast iron produced in the smelting furnace is oxidized in a converter to obtain blister copper. This flow is shown in Fig. 3.
本発明法による還元によりマグネタイトが還元されてF
eOが形成されるので、必要に応じ5i02等のフラッ
クスを還元剤と同時に吹込むか。Magnetite is reduced by the reduction method of the present invention and F
Since eO is formed, if necessary, can a flux such as 5i02 be injected at the same time as the reducing agent?
又は別途装入して転炉錫組成の調整を行なう。Or charge it separately and adjust the converter tin composition.
ここでは還元剤として微粉炭を例示したが、コークス等
の他の固体還元剤を使用してもよく、更に重油等の液体
還元剤や1.P、G、 、アンモニア等の気体還元剤
でもよい。Although pulverized coal is used as an example of the reducing agent here, other solid reducing agents such as coke may also be used, and liquid reducing agents such as heavy oil or 1. A gaseous reducing agent such as P, G, or ammonia may also be used.
次に、浮遊選鉱法を組込んだ従来の銅転炉幼の処理法の
結果の一例を第1表に示す。Next, Table 1 shows an example of the results of the conventional copper converter treatment method incorporating the flotation method.
(以下余白)
第1表
また、銅転炉訪を溶体のまま溶錬炉やセットリング炉等
へ繰返し、コークス等を上から添加して転炉跡の溶体F
に浮遊させ、溶体表面の酸化、固化を防止しながら転炉
訪中の鋳と鋳を相尾分離させる従来法による処理結果の
一例を第2表に示す。(Left below) Table 1 In addition, the copper converter is repeatedly visited as a melt into a smelting furnace, settling furnace, etc., and coke, etc. is added from above, and the solution F
Table 2 shows an example of the treatment results using the conventional method of separating the castings from the converter while preventing oxidation and solidification of the solution surface.
(以下余白)
第2表
!
次に、溶体状の銅転炉拐をセットリング炉へ装入した後
、還元剤である微粉炭を該溶体内へ吹込み、マグネタイ
トを還元することにより該溶体中の鋳と語との相星分離
を促進する本発明法による処理結果を第3表に示す。(Left below) Table 2! Next, after charging the copper converter powder in a solution state into a settling furnace, pulverized coal as a reducing agent is blown into the solution to reduce the magnetite, thereby reducing the phase of the copper converter in the solution. Table 3 shows the results of the treatment according to the method of the present invention that promotes star separation.
また、上記還元剤の吹込み砥と転炉訪中の銅品位の関係
を第4図に示す。Moreover, the relationship between the blowing grinding of the reducing agent and the copper quality during the visit to the converter is shown in FIG.
(以下余白)
第 3 表
(微粉炭: 6X10−3t/を転炉tル使用時)(ニ
)発明の効果
l―記の如く1本発明法によれば、銅製錬工程で発生す
る鎚が混入した転炉拐から低コストで収率よく鶏を分離
回収できる利点がある。(Leaving space below) Table 3 (Pulverized coal: 6 x 10-3 tons/ton used in a converter) This method has the advantage of being able to separate and recover chickens from contaminated converter scraps at low cost and with high yield.
第1〜2図は従来の銅精鉱の処理工程を示すフローシー
ト、第3図は本発明法を適用した銅精鉱の処理工程の一
例を示すフローシート、第4図は溶体状の銅転炉拐に微
粉炭を吹込んだ場合の水砕を男(生成跡)中の銅品位と
微粉炭吹込量との関係ならびに上記溶体I−にコークス
を添加する従来法による水砕訪中の銅品位の変化の比較
を示すグラフである。
特 許 出 願 人 同和鉱業株式会社代 理 人
弁理士 浅 賀 −大同 弁理士
浅 賀 −樹第1図
第2図
第3図Figures 1 and 2 are flow sheets showing conventional processing steps for copper concentrate, Figure 3 is a flow sheet showing an example of processing steps for copper concentrate to which the method of the present invention is applied, and Figure 4 is a flow sheet showing copper concentrate in solution. The relationship between the copper grade in the pulverized coal and the amount of pulverized coal injected when pulverized coal is injected into the converter, and the relationship between the copper quality in the pulverized coal and the amount of pulverized coal injected into the converter, as well as the relationship between the amount of pulverized coal and the amount of pulverized coal injected into the molten coal. It is a graph showing a comparison of changes in quality. Patent applicant Dowa Mining Co., Ltd. Agent Patent attorney Asaga - Daido Patent attorney
Asaga - Tree Figure 1 Figure 2 Figure 3
Claims (1)
剤を該溶体内へ吹込んでマグネタイトを還元することに
より、該溶体中の■と■との相互分離を促進することを
特徴とする銅転炉■の処理法。After charging the copper converter (■) in solution form into a settling furnace, a reducing agent is injected into the solution to reduce magnetite, thereby promoting mutual separation of (1) and (2) in the solution. Treatment method for copper converter ■.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15941685A JPS6220841A (en) | 1985-07-19 | 1985-07-19 | Treatment of copper converter slag |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15941685A JPS6220841A (en) | 1985-07-19 | 1985-07-19 | Treatment of copper converter slag |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6220841A true JPS6220841A (en) | 1987-01-29 |
Family
ID=15693267
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15941685A Pending JPS6220841A (en) | 1985-07-19 | 1985-07-19 | Treatment of copper converter slag |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6220841A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6436169B2 (en) * | 2000-03-03 | 2002-08-20 | Nippon Mining & Metals Co., Ltd. | Method of operating a copper smelting furnace |
JP2002363659A (en) * | 2001-06-04 | 2002-12-18 | Nippon Mining & Metals Co Ltd | Device for charging material containing iron in copper smelting furnace |
JP2004011011A (en) * | 2002-06-11 | 2004-01-15 | Nippon Mining & Metals Co Ltd | Method of recovering cooper from cooper converter slag |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS503917A (en) * | 1973-05-17 | 1975-01-16 | ||
JPS58177421A (en) * | 1982-04-07 | 1983-10-18 | エスケーエフ スティール エンジニアリング アクティエボラーグ | Recovery of metal from molten slag |
-
1985
- 1985-07-19 JP JP15941685A patent/JPS6220841A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS503917A (en) * | 1973-05-17 | 1975-01-16 | ||
JPS58177421A (en) * | 1982-04-07 | 1983-10-18 | エスケーエフ スティール エンジニアリング アクティエボラーグ | Recovery of metal from molten slag |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6436169B2 (en) * | 2000-03-03 | 2002-08-20 | Nippon Mining & Metals Co., Ltd. | Method of operating a copper smelting furnace |
JP2002363659A (en) * | 2001-06-04 | 2002-12-18 | Nippon Mining & Metals Co Ltd | Device for charging material containing iron in copper smelting furnace |
JP2004011011A (en) * | 2002-06-11 | 2004-01-15 | Nippon Mining & Metals Co Ltd | Method of recovering cooper from cooper converter slag |
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