JPS6075533A - Method for operating oxidation and reduction furnace - Google Patents

Method for operating oxidation and reduction furnace

Info

Publication number
JPS6075533A
JPS6075533A JP18084983A JP18084983A JPS6075533A JP S6075533 A JPS6075533 A JP S6075533A JP 18084983 A JP18084983 A JP 18084983A JP 18084983 A JP18084983 A JP 18084983A JP S6075533 A JPS6075533 A JP S6075533A
Authority
JP
Japan
Prior art keywords
tuyeres
tuyere
oxidation
reduction
furnace
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.)
Granted
Application number
JP18084983A
Other languages
Japanese (ja)
Other versions
JPH0350806B2 (en
Inventor
Masanori Kato
正憲 加藤
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.)
Eneos Corp
Original Assignee
Nippon Mining 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 Nippon Mining Co Ltd filed Critical Nippon Mining Co Ltd
Priority to JP18084983A priority Critical patent/JPS6075533A/en
Publication of JPS6075533A publication Critical patent/JPS6075533A/en
Publication of JPH0350806B2 publication Critical patent/JPH0350806B2/ja
Granted legal-status Critical Current

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  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Furnace Charging Or Discharging (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To improve the work efficiency of oxidation and reduction of molten metal in an oxidation and reduction furnace by attaching plural tuyeres of different kinds to the furnace so that they are arranged under the surface of the bath and by carrying out each of oxidation, slag discharge and reduction stages with tuyeres suitable for the stage after plugging other tuyeres. CONSTITUTION:Tuyere groups each consisting of a tuyere 1 of a large diameter and a tuyere 2 of a small diameter are attached to plural positions of a furnace for oxidizing and reducing molten metal such as a refining furnace 3 so that they are arranged under the surface of the bath. In an oxidation stage, the tuyeres 2 are plugged with plugging members 12, and a large volume of air is blown from the tuyeres 1. In a reduction stage, the tuyeres 1 are plugged with plugging members 11, and heavy oil or the like is blown from the tuyeres 2 to remove oxygen.

Description

【発明の詳細な説明】 この発明は、金属溶体全酸化還元する炉の操業法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for operating a furnace for total redox of metal solutions.

金属溶体ケ酸化還元する炉、たとえば銅の精製炉は、酸
化剤および還元剤を吹込む酸化・還元用羽口金有してお
り、酸化工程では一般に羽口力・ら直接溶鋼中に空気を
吹込みイオウを酸化除去し。
Furnaces that oxidize and reduce metal solutions, such as copper refining furnaces, have tuyeres for oxidation and reduction that blow oxidizing and reducing agents into the molten steel. Removes sulfur by oxidation.

さらに溶剤を吹込む等により粗銅中の不純物vr[とじ
て除去する。つぎの還元工程では燃料と空気の混合物な
ど全前記同じ羽口がら吹込み酸素を除去するようにして
いる。
Furthermore, impurities in the blister copper are removed by blowing in a solvent or the like. The next reduction step involves removing the blown oxygen from the same tuyeres, including a mixture of fuel and air.

ところが、従来の羽口では、上述のように空気と燃料と
を還元雰囲気となるべく混合して吹込むためその構造上
あまり大径にできない。したがって、溶銅におけるイオ
ウの含有率が大きい場合に。
However, in the conventional tuyeres, as mentioned above, air and fuel are mixed and blown into the tuyere to create a reducing atmosphere, so the diameter cannot be made very large due to its structure. Therefore, when the content of sulfur in molten copper is large.

従来の羽口では空気を大量に吹込めないなどの問題があ
る。
Conventional tuyeres have problems such as the inability to blow in large amounts of air.

また、跋排出を羽目を利用し、倭全排出口に送るので、
羽口位置も非常に限定される。
In addition, since the waste is sent to the Wazen discharge port by utilizing the waste,
Tuyere locations are also very limited.

この発明は、以上の点に鑑みてなされたものであって、
すなわちこの発明は、酸化工程の際に大量の酸化剤が吹
込めると共に、酸化工程から還元工程、さらに還元工程
から次の回分の酸化工程に移る際に酸化剤・還元剤供給
の切換え全スムーズに行なうことができる酸化還元炉の
操業法を提供することを目的とする。
This invention was made in view of the above points, and
In other words, this invention allows a large amount of oxidizing agent to be injected during the oxidation process, and also enables smooth switching of the oxidizing agent/reducing agent supply when moving from the oxidation process to the reduction process and then from the reduction process to the next batch of oxidation process. The purpose of this invention is to provide a method for operating a redox furnace that can be carried out.

したがって、この目的全達成するためにこの発明の酸化
還元炉の操業法は、金属溶体を酸化還元する炉に種々の
異なる複数個の羽ロケ同時に浴面下になるように配置す
る場合において、酸化、薮排出、還元等する工程全行な
うときは、各々の工程に適した羽口を選択使用すると共
にその他の羽口全閉そくすること全特徴とする。
Therefore, in order to achieve all of these objectives, the operating method of the redox furnace of the present invention is such that when a plurality of various blades are placed in a furnace for redoxing a metal solution so as to be under the bath surface at the same time, When carrying out all processes such as bush discharge, reduction, etc., the tuyere suitable for each process should be selected and used, and the other tuyere should be completely closed.

以下、図示の一実施例によりこの発明全説明する。The present invention will be fully explained below with reference to an embodiment shown in the drawings.

第1図は、この発明全説明するのに用いる精製炉の概略
図、第2図(ト)(I3)は、酸化工程全説明するため
の精製炉の羽口部の断面図、第3図(A)(B)は還元
工程全説明するための精製炉の羽口部の断面図である。
Figure 1 is a schematic diagram of a refining furnace used to fully explain this invention, Figures 2 (G) and (I3) are sectional views of the tuyere portion of the refining furnace used to fully explain the oxidation process, and Figure 3 (A) and (B) are cross-sectional views of the tuyere portion of the refining furnace for explaining the entire reduction process.

第1図に示す金属溶体を酸化還元する炉としてのたとえ
ば精製炉は、横型傾転タイプのものであり、太径50晒
φの羽口1と小径たとえば15欄φの羽口2工り成る羽
口群が多数設けられている。
For example, the refining furnace as a furnace for redoxing a metal solution shown in Fig. 1 is of a horizontal tilting type, and consists of a tuyere 1 with a large diameter of 50 mm and 2 tuyeres with a small diameter of, for example, 15 column φ. There are many tuyere groups.

この精製炉の炉シェル3の内周面には、第2図(5)(
r+)に示す工うに耐火レンガ4が内張りされている。
The inner circumferential surface of the furnace shell 3 of this refining furnace is
The wall shown in r+) is lined with refractory bricks 4.

前記大径および小径の羽口1,2の羽口管5,6は、好
ましくは精製炉内の溶体の溶解温度より高い融点?有す
る利料たとえば鉄でできており、その各内方開口端7,
8は前記耐火レンガ4の内周面i/i:まで達している
と共に、各外方装入端9,10は炉シェル3エリ外方に
突出されている。
The tuyere tubes 5, 6 of the large and small diameter tuyeres 1, 2 preferably have a melting point higher than the melting temperature of the melt in the refining furnace. each inner open end 7,
8 reaches the inner circumferential surface i/i: of the refractory brick 4, and each outer charging end 9, 10 projects outward from the furnace shell 3 area.

一方、第1Nに示す1.1 、12は、前記羽目管5.
6を閉そくするのに用いる大径および小径の閉そく用部
材である。詳細には、大径の閉そく用部材11は、第3
図(13)に示すように前記羽口管5と同様にたとえば
鉄で作られた羽口内管13と、この羽口内管13内に充
填された不定形耐火物(たとえばキャスタブルなど)1
4とを有1−でいる。この羽口内管13の外周には、該
羽口内管13と羽口管5とのギャップ(たとえば2.5
 mm程度)をうめ、力)つ羽1]管5への装入あるい
は取ジ出し全容易にする潤滑材料、たとえば水ガラスあ
るいはグラファイト等が必要に応じてコーティングされ
ている。
On the other hand, 1.1 and 12 shown in No. 1N are the panel pipes 5.
These are large-diameter and small-diameter blocking members used to block 6. In detail, the large-diameter blocking member 11 is
As shown in FIG. 13, there is a tuyere inner tube 13 made of iron, for example, similar to the tuyere tube 5, and a monolithic refractory (for example, castable) 1 filled in the tuyere inner tube 13.
4 and 1-. A gap (for example, 2.5
If necessary, it is coated with a lubricating material such as water glass or graphite to facilitate loading or unloading into the tube 5.

また、前記小径の閉そく用部材12は、第2図(ト)に
示すように前記閉そく用部材11と同様の構成であり、
羽口内管15内には不定形耐火物16が充填されている
と共に、必要に応じて羽口内管15の外周には潤滑材料
がコーティングされている。
Further, the small-diameter blocking member 12 has the same configuration as the blocking member 11, as shown in FIG. 2 (G),
The tuyere inner tube 15 is filled with a monolithic refractory 16, and the outer periphery of the tuyere inner tube 15 is coated with a lubricating material as required.

しかして、精製炉全操業している状態において、まず酸
化工程について説明する。
First, the oxidation process will be explained while the refining furnace is in full operation.

酸化工程においては、第2図(A)に示すように小径の
羽1]20羽目管6に対して、外方装入端10工り小径
の閉そく用部材12を装入して羽口管6を閉そくすると
共に、第2図(13)VC示すように大径の羽目10羽
口管5は開放しておく。そして、羽目管5よジ大量の空
気全吹込み、たとえば精製炉内の溶体(たとえば溶鋼)
中に含まれるイオウ全過酸化することで除去する。上記
酸化処理が終了すると、前記閉そく用部材12を押して
精製炉内に落しこみあるいは抜き出して小径の羽目管6
を開放する。
In the oxidation process, as shown in FIG. 2(A), a small-diameter blocking member 12 with a 10-cut outer charging end is charged into the small-diameter blade 1 and 20-window tube 6 to form a tuyere tube. 6 is closed, and the large-diameter tuyere pipe 5 with 10 large-diameter slats 5 is left open as shown in FIG. 2 (13) VC. Then, a large amount of air is completely blown through the siding pipe 5, for example, to melt the liquid (such as molten steel) in the refining furnace.
The sulfur contained in it is removed by total peroxidation. When the oxidation treatment is completed, the blocking member 12 is pushed and dropped into the refining furnace or pulled out and the small-diameter siding tube 6 is inserted into the refining furnace.
to open.

次に、還元工程においては、前述とは逆に第3図(5)
に示すように小径の羽口2の羽口管6は開放しておくと
共に、第3図fB)に示すように大径の羽目10羽目管
5に対して、外方装入端9.r、り大径の閉そく用部材
11全装入して羽目管5を閉そくする。そして1羽口管
6エり重油など全吹込み。
Next, in the reduction process, contrary to the above, as shown in Fig. 3 (5)
As shown in FIG. 3, the tuyere tube 6 of the small diameter tuyere 2 is left open, and the outer charging end 9. r, the large-diameter blocking member 11 is fully charged and the siding pipe 5 is blocked. Then, one tuyere tube with 6 holes is fully injected with heavy oil.

酸素の除去を行々う。この還元処理が終了(−1操業が
次の回分に移り、再び酸化工程になれば、羽目管6を閉
そくして羽口管5全開放すればよい。
Let's remove oxygen. When this reduction process is completed (-1) and the operation moves on to the next batch and the oxidation process starts again, the tuyere pipe 6 may be closed and the tuyere pipe 5 may be completely opened.

上述した要領で酸化および還元工程において操作するこ
とで、酸化工程の際に大量の酸化剤が吹込めると共に、
酸化工程から鏝排出、還元工程、さらに還元工程から次
の回分の酸化工程に移る際に酸化剤、還元剤供給の切換
えをスムーズに行なうことができる。
By operating in the oxidation and reduction steps as described above, a large amount of oxidizing agent can be injected during the oxidation step, and
When moving from the oxidation process to the trowel discharge to the reduction process, and further from the reduction process to the next batch of oxidation process, the supply of oxidizing agent and reducing agent can be smoothly switched.

ところで、本実施例では金属置体全酸化還元する炉とし
て銅の精製炉をとりあげたが、これに限らずこの発明の
方法は種々の炉に適用できることはいうまでもない。
Incidentally, in this embodiment, a copper refining furnace was used as the furnace for performing total oxidation and reduction of metal bodies, but it goes without saying that the method of the present invention is not limited to this and can be applied to various furnaces.

以上説明したようにこの発明(Cよれば、酸化。As explained above, this invention (according to C, oxidation.

緩排出、還元等の工程を行なうときは各々の工程に適し
た羽口を選択使用すると共にその他の羽口全閉そくする
ので、酸化工程の際に大量の酸化剤が吹込めると共に、
酸化工程から還元工程、さらに還元工程から次の回分の
酸化工程に移る際に酸化剤、還元剤供給の切換え全スム
ーズに行なうことができ、溶体の酸化還元作業性全向上
できる効果がある。
When performing processes such as slow discharge and reduction, the tuyere suitable for each process is selected and the other tuyeres are completely closed, so a large amount of oxidant can be injected during the oxidation process, and
When moving from the oxidation step to the reduction step and further from the reduction step to the next batch of oxidation steps, the supply of oxidizing agent and reducing agent can be switched completely smoothly, which has the effect of completely improving the redox workability of the solution.

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

第1図は、この発明全説明するのに用いる精製炉の概略
図、第2図(5)(I3)は、酸化工程全説明するため
の精製炉の羽口部の断面図、第3図(5)03)は還元
工程全説明するための精製炉の羽口部の断面図である。 1・・大径の羽目、2・・・小径の羽目、11 ・・大
径の羽口の閉そく用部材、12・・・小径の羽口の閉そ
く用部材。 特許出願人 日本鉱業株式会社 代理人 弁理士 西 村 教 光 第1図
Figure 1 is a schematic diagram of a refining furnace used to fully explain this invention, Figures 2 (5) and (I3) are cross-sectional views of the tuyere of the refining furnace used to fully explain the oxidation process, and Figure 3 (5)03) is a sectional view of the tuyere portion of the refining furnace for explaining the entire reduction process. 1...Large diameter tuyere, 2...Small diameter tuyere, 11...Large diameter tuyere blocking member, 12...Small diameter tuyere blocking member. Patent applicant Nippon Mining Co., Ltd. Agent Patent attorney Norihiro Nishimura Figure 1

Claims (1)

【特許請求の範囲】[Claims] 金属溶体′に酸化還元する炉に種類の異なる複数個の羽
口全同時に浴面下になるように配置する場合において、
酸化、薮排出、還元等の工程全行々うときは各々の工程
に適した羽口を選択使用すると共に、その他の羽口を閉
そくすること全特徴とする酸化還元炉の操業法。
When multiple tuyeres of different types are placed in a furnace for redoxing a metal solution so that they are all under the bath surface at the same time,
A method of operating an oxidation-reduction furnace characterized by selecting and using tuyeres suitable for each process when performing all processes such as oxidation, bush discharge, and reduction, and closing other tuyeres.
JP18084983A 1983-09-30 1983-09-30 Method for operating oxidation and reduction furnace Granted JPS6075533A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18084983A JPS6075533A (en) 1983-09-30 1983-09-30 Method for operating oxidation and reduction furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18084983A JPS6075533A (en) 1983-09-30 1983-09-30 Method for operating oxidation and reduction furnace

Publications (2)

Publication Number Publication Date
JPS6075533A true JPS6075533A (en) 1985-04-27
JPH0350806B2 JPH0350806B2 (en) 1991-08-02

Family

ID=16090430

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18084983A Granted JPS6075533A (en) 1983-09-30 1983-09-30 Method for operating oxidation and reduction furnace

Country Status (1)

Country Link
JP (1) JPS6075533A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07102004B2 (en) * 1989-09-27 1995-11-08 株式会社クボタ Steering controller for reaper harvester

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55138029A (en) * 1979-03-27 1980-10-28 Liquid Air Canada Conversion of nonferrous metal regulus
JPS58180851A (en) * 1982-04-16 1983-10-22 Mitsubishi Heavy Ind Ltd Apparatus for damping vibration of mechanical structure

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55138029A (en) * 1979-03-27 1980-10-28 Liquid Air Canada Conversion of nonferrous metal regulus
JPS58180851A (en) * 1982-04-16 1983-10-22 Mitsubishi Heavy Ind Ltd Apparatus for damping vibration of mechanical structure

Also Published As

Publication number Publication date
JPH0350806B2 (en) 1991-08-02

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