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JP3528553B2 - Removal method of residual solution in copper making furnace - Google Patents
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JP3528553B2 - Removal method of residual solution in copper making furnace - Google Patents

Removal method of residual solution in copper making furnace

Info

Publication number
JP3528553B2
JP3528553B2 JP34978697A JP34978697A JP3528553B2 JP 3528553 B2 JP3528553 B2 JP 3528553B2 JP 34978697 A JP34978697 A JP 34978697A JP 34978697 A JP34978697 A JP 34978697A JP 3528553 B2 JP3528553 B2 JP 3528553B2
Authority
JP
Japan
Prior art keywords
solution
furnace
copper
lance
oxygen
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 - Lifetime
Application number
JP34978697A
Other languages
Japanese (ja)
Other versions
JPH11181534A (en
Inventor
望 長谷川
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 JP34978697A priority Critical patent/JP3528553B2/en
Publication of JPH11181534A publication Critical patent/JPH11181534A/en
Application granted granted Critical
Publication of JP3528553B2 publication Critical patent/JP3528553B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Manufacture And Refinement Of Metals (AREA)
  • Furnace Housings, Linings, Walls, And Ceilings (AREA)
  • Furnace Charging Or Discharging (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、定置型製銅炉の炉
修理に際して、炉床煉瓦の点検あるいは解体、積替を行
うために炉底部に残留している溶体を除去する製銅炉に
おける残留溶体の除去方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a copper-making furnace for removing a molten metal remaining at the bottom of a furnace for inspecting, disassembling, or transshipping hearth bricks when repairing a stationary copper-making furnace. The present invention relates to a method for removing residual solution.

【0002】[0002]

【従来の技術】例えば、銅精鉱の連続製錬方法において
硫化金属鉱を精錬する場合には、図1に示すように、ま
ず、溶錬炉1において銅精鉱を溶融して、硫化銅及び硫
化鉄を主成分とするカワMと、原料中の脈石や溶剤や酸
化鉄等を主成分とするカラミSとを生成し、次いで、分
離炉2においてカラミSとカワMとを分離し、続いて、
製銅炉3においてカワMを酸化させて粗銅Cとし、さら
に、精製炉4において上記粗銅Cを精製して、より銅品
位の高い精製銅を生成するようにしている。そして、上
記溶錬炉1と製銅炉3には、二重管構造を有するランス
5a,5bがこれらの炉の天井を挿通して昇降自在に設
けられており、これらのランス5a,5bを介して銅精
鉱、酸素富化空気、溶剤、冷剤等が各炉内に供給されて
いる。また、上記分離炉2は例えば電極6を備えた電気
炉である。そして、これらの溶錬炉1、分離炉2及び製
銅炉3は、この順に高低差が付けられていると共に、溶
体の流路である樋7a,7bによって連絡されている。
2. Description of the Related Art For example, in the case of refining a metal sulfide ore in a continuous smelting method of a copper concentrate, first, as shown in FIG. And Kawa M containing iron sulfide as a main component, and Karami S containing gangue, a solvent, iron oxide, etc. in the raw material as main components, and then separating the Karami S and the Kawa M in the separation furnace 2. ,continue,
The copper M is oxidized in the copper-making furnace 3 to obtain crude copper C, and the crude copper C is further purified in the refining furnace 4 to produce refined copper having a higher copper grade. Then, the smelting furnace 1 and the copper-making furnace 3 are provided with lances 5a and 5b having a double pipe structure so as to be vertically movable through the ceilings of these furnaces. Copper concentrate, oxygen-enriched air, solvent, cooling agent, etc. are supplied to each furnace via the above. The separation furnace 2 is an electric furnace equipped with an electrode 6, for example. The smelting furnace 1, the separating furnace 2 and the copper-making furnace 3 are provided with a height difference in this order, and are connected by gutters 7a and 7b which are flow paths for the solution.

【0003】[0003]

【発明が解決しようとする課題】ところで、上記溶錬炉
1あるいは製銅炉3のような製錬炉には、炉修理の際に
炉底部に残留している溶体を抜き出すために底抜き装置
が設置されている(例えば、特願平2−314680号
参照)。しかしながら、この底抜き装置を使用しても、
完全に炉内部の溶体を抜き出すことは難しいという問題
があった。そして、従来、炉底部に残留して抜き出せな
い溶体については、この溶体を冷却固化させた後、作業
員の人手に頼って機械的な手段により除去していた。こ
の場合、残留溶体が粗銅である製銅炉3にあっては、簡
単に残留溶体を除去することが難しく、ジェットランス
によって残留溶体を溶断して除去するようにしている
が、この作業は時間がかかり、労力を要すると共に、作
業環境が悪く作業員に負担がかかるという問題があっ
た。また、上記製銅炉3においては、上記残留溶体を炉
床から簡単に引き離すことができないから、炉床状態の
点検を行うことができないという不満があった。本発明
は、上記事情に鑑みてなされたもので、その目的とする
ところは、残留溶体を容易に炉底部から除去することが
できて、炉床の解体、炉床煉瓦の積替作業を簡単に行う
ことができて、炉操業率の大幅な向上を図ることができ
ると共に、作業員にかかる負担を大幅に低減することが
できる一方、炉床の点検作業を円滑にかつ確実に行うこ
とができる製銅炉における残留溶体の除去方法を提供す
ることにある。
By the way, in a smelting furnace such as the smelting furnace 1 or the copper smelting furnace 3 described above, there is a bottom removing device for extracting the solution remaining at the bottom of the furnace when the furnace is repaired. Is installed (for example, see Japanese Patent Application No. 2-314680). However, even if this bottoming device is used,
There was a problem that it was difficult to completely extract the molten metal inside the furnace. Then, conventionally, for the solution that remains at the bottom of the furnace and cannot be extracted, after cooling and solidifying the solution, the solution was removed by mechanical means relying on the workers. In this case, in the copper-making furnace 3 in which the residual solution is crude copper, it is difficult to easily remove the residual solution, and the jet lance is used to melt and remove the residual solution. However, there is a problem in that the work environment is poor, the work environment is bad, and the worker is burdened. Further, in the copper-making furnace 3, there has been a complaint that the state of the hearth cannot be inspected because the residual solution cannot be easily separated from the hearth. The present invention has been made in view of the above circumstances, and an object thereof is to easily remove a residual solution from the bottom of a furnace, and to easily dismantle a hearth and to transfer a hearth brick. The furnace operation rate can be significantly improved, and the burden on workers can be significantly reduced, while the hearth inspection work can be performed smoothly and reliably. It is an object of the present invention to provide a method for removing a residual solution in a copper manufacturing furnace that can be performed.

【0004】[0004]

【課題を解決するための手段】本発明の請求項1は、炉
床煉瓦の点検あるいは解体、積替を行う際に、炉底部に
残留している溶体を除去する製銅炉における残留溶体の
除去方法であって、上記溶体を上記炉底部から抜き出す
に際して、上記溶体の上方からランスによって酸素富化
空気を吹き付け、上記残留溶体の少なくとも一部をカラ
ミ化するものである。これにより、炉底部に残留してい
る溶体に積極的に酸素を供給してこの溶体を酸化、カラ
ミ化すると共に、溶体を効果的に攪拌して溶体各部の温
度を均一に上昇させ溶体を炉底部からできるだけ抜き出
す。また、本発明の請求項2は、上記ランス高さを溶体
面から0.5〜2mに設定したものである。このように
設定したのは、ランス高さが0.5mよりも低いと、ス
プラッシュによってランスが閉塞する恐れがあると共
に、炉床の点検作業だけを行う場合に、炉床煉瓦を損傷
する恐れがある一方、ランス高さが2mよりも高いと、
反応効率が低下して、十分な反応が得られずに溶体が冷
却固化してしまうからである。さらに、本発明の請求項
3は、上記ランスによって吹き付ける酸素富化空気の酸
素濃度を40〜70%に設定したものである。このよう
に設定したのは、酸素濃度が40%よりも低いと、十分
に反応せずに溶体が固化してしまう一方、酸素濃度が7
0%よりも高いと、反応熱が高く、ランスが溶損する恐
れが大きいからである。さらにまた、本発明の請求項4
は、上記ランスによって吹き付ける酸素富化空気の流速
を130〜150Nm/sに設定したものである。この
ように設定したのは、酸素富化空気の流速が130Nm
/sよりも低いと、所要の反応効率を確保できなくなる
と共に、溶体を十分に攪拌することができない一方、酸
素富化空気の流速が150Nm/sよりも高いと、スプ
ラッシュによる冷却ジャケットの溶損を引き起こす恐れ
があると共に、炉床点検だけを行う場合に、炉床を損傷
する恐れがあるからである。また、本発明の請求項5
は、上記炉底部から溶体を抜き出すに際して、バーナー
により炉内部を加熱するものである。これにより、炉内
の雰囲気を暖めて溶体の酸化反応を促進すると共に、炉
壁に付着したスプラッシュを溶かして炉底部の溶体中に
落とす。なおまた、本発明の請求項6は、酸素富化空気
を溶体に吹き付けた後、この溶体を冷却固化させて、こ
の固化した溶体を破砕して除去するものである。この場
合、上記残留溶体が十分に酸化、カラミ化しているか
ら、固化した溶体はもろくかつ破砕し易い。
According to claim 1 of the present invention, when inspecting, disassembling, or transshipping a hearth brick, the residual solution in a copper-making furnace is removed to remove the solution remaining in the bottom of the furnace. A removal method, wherein when the solution is extracted from the bottom of the furnace, oxygen-enriched air is blown from above the solution with a lance so that at least a part of the residual solution is colored.
Is shall be Mi of. As a result, oxygen is positively supplied to the solution remaining at the bottom of the furnace to oxidize and caramize the solution, and the solution is effectively stirred to uniformly raise the temperature of each part of the solution and remove the solution from the furnace. Pull out from the bottom as much as possible. According to the second aspect of the present invention, the lance height is set to 0.5 to 2 m from the solution surface. If the height of the lance is less than 0.5 m, the lance may be blocked by the splash and the hearth bricks may be damaged when only the hearth inspection work is performed. On the other hand, if the lance height is higher than 2 m,
This is because the reaction efficiency is lowered and the solution is cooled and solidified without sufficient reaction. Furthermore, the third aspect of the present invention sets the oxygen concentration of the oxygen-enriched air blown by the lance to 40 to 70%. The reason for this setting is that when the oxygen concentration is lower than 40%, the solution does not react sufficiently and the solution solidifies, while the oxygen concentration is 7%.
This is because if it is higher than 0%, the reaction heat is high and the lance is liable to melt. Furthermore, claim 4 of the present invention
Is the one in which the flow rate of the oxygen-enriched air blown by the lance is set to 130 to 150 Nm / s. The setting was made so that the flow rate of oxygen-enriched air was 130 Nm.
If it is lower than / s, the required reaction efficiency cannot be ensured, and the solution cannot be sufficiently stirred. On the other hand, if the flow rate of oxygen-enriched air is higher than 150 Nm / s, the cooling jacket will melt due to splashing This is because there is a risk of causing a fire and damage to the hearth when only the hearth is inspected. Further, claim 5 of the present invention
Is for heating the inside of the furnace by a burner when extracting the solution from the bottom of the furnace. As a result, the atmosphere in the furnace is warmed to accelerate the oxidation reaction of the solution, and the splash adhered to the furnace wall is melted and dropped into the solution at the bottom of the furnace. Still further, the sixth aspect of the present invention is to blow oxygen-enriched air onto the solution, cool and solidify the solution, and crush and remove the solidified solution. In this case, since the above-mentioned residual solution has been sufficiently oxidized and caramized, the solidified solution is fragile and easily crushed.

【0005】[0005]

【発明の実施の形態】以下、図1を参照して、本発明の
実施の形態を説明する。製銅炉3の炉底部に形成された
底抜き口10から溶体を抜き出す作業に引き続き、通常
操業に使用している8本のランス5bのうち炉中心に比
較的近い2〜5本のランス5bをそのまま使用すると共
に、溶体面が低下していることに対応して上記各ランス
5bの高さを再調整し、これらのランス5bから通常操
業と同程度のガス流速及び通常より高めの酸素濃度で送
風し、炉底部に残留している溶体を酸化する。また、必
要に応じて、重油バーナーによる助燃(炉内雰囲気の加
熱)を行うが、この場合、フラックスの添加は不要であ
る。上記各ランス5bの高さは、溶体面から0.5〜2
mに設定されている。この理由は、ランス高さが0.5
mよりも低いと、ランス5bが溶体面に近づき過ぎるた
めに、スプラッシュによってランス5bが閉塞する恐れ
があると共に、炉床の点検だけを行う場合に、炉床煉瓦
が損傷する恐れがあるからである。また、ランス高さが
2mよりも高いと、反応効率が低下して、十分に溶体の
温度を上昇させることができず、溶体が冷却固化するか
らである。上記ランス5bによって吹き付ける酸素富化
空気の酸素濃度は、40〜70%に設定されている。こ
の理由は、酸素濃度が40%よりも低いと、十分に反応
せずに溶体が固化してしまう一方、酸素濃度が70%よ
りも高いと、反応熱が高く、ランス5bが溶損する恐れ
が大きいからである。上記ランス5bによって吹き付け
る酸素富化空気の流速は130〜150Nm/sに設定
されている。この理由は、酸素富化空気の流速が130
Nm/sよりも低いと、所要の反応効率を確保できなく
なると共に、溶体を十分に攪拌することができないから
であり、酸素富化空気の流速が150Nm/sよりも高
いと、スプラッシュによる冷却ジャケットの溶損を引き
起こす恐れがあると共に、炉床点検だけを行う場合に、
炉床を損傷する恐れがあるからである。
DETAILED DESCRIPTION OF THE INVENTION An embodiment of the present invention will be described below with reference to FIG. Subsequent to the work of extracting the solution from the bottom outlet 10 formed at the bottom of the copper-making furnace 3, 2 to 5 lances 5b relatively close to the center of the furnace out of the 8 lances 5b used for normal operation Is used as it is, and the height of each of the above-mentioned lances 5b is readjusted in response to the decrease in the solution surface. To blow air to oxidize the solution remaining on the bottom of the furnace. Further, if necessary, auxiliary combustion by a heavy oil burner (heating of the atmosphere in the furnace) is performed, but in this case, addition of flux is unnecessary. The height of each lance 5b is 0.5 to 2 from the solution surface.
It is set to m. The reason for this is that the lance height is 0.5.
If it is lower than m, the lance 5b may come too close to the solution surface, and the splash may block the lance 5b, and the hearth brick may be damaged when only the hearth is inspected. is there. Further, if the lance height is higher than 2 m, the reaction efficiency is lowered, the temperature of the solution cannot be sufficiently raised, and the solution is cooled and solidified. The oxygen concentration of the oxygen-enriched air blown by the lance 5b is set to 40 to 70%. The reason for this is that when the oxygen concentration is lower than 40%, the solution solidifies without sufficient reaction, while when the oxygen concentration is higher than 70%, the reaction heat is high and the lance 5b may be melted and damaged. Because it is big. The flow velocity of the oxygen-enriched air blown by the lance 5b is set to 130 to 150 Nm / s. The reason for this is that the flow rate of oxygen-enriched air is 130
This is because if it is lower than Nm / s, the required reaction efficiency cannot be ensured and the solution cannot be sufficiently stirred, and if the flow rate of oxygen-enriched air is higher than 150 Nm / s, the cooling jacket due to splashing. If there is a risk of causing melting damage of the
This is because the hearth may be damaged.

【0006】このようにして、ランス5bを用いて溶体
に酸素富化空気を吹き付けると、該溶体が酸化、カラミ
化すると共に、溶体が攪拌されることにより、溶体各部
の温度が均一化して底抜き口10から溶体を抜き出し易
くなる。従って、従来に比べて炉底部に残留する溶体の
量を少なく抑制できる。次いで、この溶体の底抜き口1
0からの抜き出し作業が終わると、炉底部になおも残留
している溶体を冷却固化させて、この固化した溶体を破
砕して除去する。この場合、上記残留溶体が十分に酸
化、カラミ化しているから、固化した溶体はもろくかつ
破砕し易く、従って、作業員が簡単に除去することがで
きる。この結果、炉床の解体が短期間に行え、かつ炉床
煉瓦の積替が円滑に行える。例えば、従来、炉床解体に
20日程度必要であったのに対して、本発明の方法によ
れば、6〜7日(約1/3)の労力にて炉床の解体が可
能となった。また、炉床の解体、積替を行わずに、炉床
の点検だけを行う場合には、作業員が酸化、カラミ化し
た残留溶体を除去するだけで、炉床の状態を目視確認す
ることができる。この場合、残留溶体の除去が容易でか
つ炉床を損傷することがないので、炉床の修理等の余分
な作業を行うことなく、炉床状態の点検だけを確実に行
うことができる。
In this manner, when oxygen-enriched air is blown onto the solution using the lance 5b, the solution is oxidized and caramelized, and the solution is agitated, so that the temperature of each part of the solution becomes uniform and the bottom of the solution becomes uniform. It becomes easy to draw out the solution from the outlet 10. Therefore, the amount of the solution remaining on the bottom of the furnace can be reduced as compared with the conventional case. Then, the bottom outlet 1 of this solution
When the work of extracting from 0 is completed, the solution still remaining on the bottom of the furnace is cooled and solidified, and the solidified solution is crushed and removed. In this case, since the above-mentioned residual solution has been sufficiently oxidized and caramized, the solidified solution is fragile and easily crushed, so that the worker can easily remove it. As a result, the hearth can be dismantled in a short period of time, and the hearth bricks can be transshipped smoothly. For example, conventionally, it took about 20 days to dismantle the hearth, but according to the method of the present invention, the hearth can be dismantled with labor of 6 to 7 days (about 1/3). It was When the hearth is to be inspected without disassembling or transshipping the hearth, the worker can visually check the condition of the hearth only by removing the residual solution that has been oxidized and decolorized. You can In this case, since the residual solution can be easily removed and the hearth is not damaged, only the inspection of the hearth state can be surely performed without performing extra work such as repairing the hearth.

【0007】[0007]

【発明の効果】本発明の請求項1は、炉床煉瓦の点検あ
るいは解体、積替を行う際に、炉底部に残留している溶
体を除去する製銅炉における残留溶体の除去方法であっ
て、上記溶体を上記炉底部から抜き出すに際して、上記
溶体の上方からランスによって酸素富化空気を吹き付
、上記残留溶体の少なくとも一部をカラミ化するもの
であるから、炉底部に残留している溶体に積極的に酸素
を供給してこの溶体を酸化、カラミ化すると共に、溶体
を効果的に攪拌することにより、溶体各部の温度を均一
に上昇させ、かつ溶体の流動性を向上させて、溶体を炉
底部から容易に抜き出すことができる。また、本発明の
請求項2によれば、上記ランス高さを溶体面から0.5
〜2mに設定することにより、スプラッシュによってラ
ンスが閉塞するのを防ぐことができると共に、炉床の点
検作業だけを行う場合に、炉床煉瓦が損傷することを防
止することができる一方、十分な反応を行わせることが
できて、溶体が冷却固化することを確実に防ぐことがで
き溶体の酸化、カラミ化を円滑に実現できる。さらに、
本発明の請求項3によれば、上記ランスによって吹き付
ける酸素富化空気の酸素濃度を40〜70%に設定した
ことにより、十分な反応熱が得られて溶体の固化を防止
することができる一方、ランスの溶損を防止することが
できて円滑にかつ確実に反応を継続することができ
る。。さらにまた、本発明の請求項4によれば、上記ラ
ンスによって吹き付ける酸素富化空気の流速を130〜
150Nm/sに設定したことにより、所要の反応効率
を容易に維持することができると共に、溶体を十分に攪
拌することができる一方、スプラッシュによる冷却ジャ
ケットの溶損を防ぐことができ、かつ炉床点検だけを行
う場合に、炉床を損傷することなく、炉底部内の溶体を
円滑に除去することができる。また、本発明の請求項5
によれば、上記炉底部から溶体を抜き出すに際して、バ
ーナーにより炉内部を加熱することにより、炉内の雰囲
気を暖めて溶体の酸化反応を促進することができ、かつ
炉内の反応を安定的に継続することができると共に、炉
壁に付着したスプラッシュを溶かして炉底部の溶体中に
落とすことができる一方、炉底部に残留する溶体の温度
を上昇させて溶体の流動性を向上させることができる。
なおまた、本発明の請求項6は、酸素富化空気を溶体に
吹き付けた後、この溶体を冷却固化させて、この固化し
た溶体を破砕して除去するものであるから、固化した残
留溶体が十分に酸化、カラミ化していることにより、固
化した溶体はもろくかつ破砕し易い。したがって、この
固化した溶体の炉底部からの除去作業を容易に行うこと
ができて、炉床を損傷することを確実に防止することが
できると共に、炉床点検並びに炉床解体、積替作業を円
滑に行うことができて、作業時間の短縮、作業人数の低
減、操業率の向上、作業者の負担の軽減等の優れた効果
を奏することができる。
EFFECT OF THE INVENTION Claim 1 of the present invention is a method for removing residual solution in a copper-making furnace, which removes the solution remaining at the bottom of the furnace when inspecting, dismantling, or transshipping the hearth bricks. Te, when extracting said solution from said furnace bottom blowing oxygen-enriched air by the lance from above the solution, because it is shall be tangled of at least part of the residual solution, remaining in the furnace bottom solution Oxygen is positively supplied to the solution to oxidize and caramize the solution, and by effectively stirring the solution, the temperature of each part of the solution is uniformly increased, and the fluidity of the solution is improved to improve the solution. Can be easily extracted from the bottom of the furnace. According to claim 2 of the present invention, the lance height is 0.5 from the solution surface.
By setting it to ~ 2 m, it is possible to prevent the lance from being blocked by the splash, and to prevent the hearth brick from being damaged when only the hearth inspection work is performed, while it is sufficient. The reaction can be carried out, the solidification of the solution can be surely prevented from cooling and solidification, and the oxidation and the caramelization of the solution can be smoothly realized. further,
According to claim 3 of the present invention, by setting the oxygen concentration of the oxygen-enriched air blown by the lance to 40 to 70%, sufficient reaction heat can be obtained to prevent solidification of the solution. Therefore, the lance can be prevented from being melted and the reaction can be smoothly and surely continued. . Furthermore, according to claim 4 of the present invention, the flow rate of the oxygen-enriched air blown by the lance is 130 to
By setting it to 150 Nm / s, the required reaction efficiency can be easily maintained, the solution can be sufficiently agitated, and the cooling jacket can be prevented from being melted by splashing, and the hearth can be prevented. When performing only the inspection, the melt in the bottom of the furnace can be smoothly removed without damaging the hearth. Further, claim 5 of the present invention
According to the above, when extracting the solution from the furnace bottom, by heating the inside of the furnace with a burner, the atmosphere in the furnace can be warmed to promote the oxidation reaction of the solution, and the reaction in the furnace can be stabilized. It is possible to continue and melt the splash adhered to the furnace wall and drop it into the solution at the bottom of the furnace, while increasing the temperature of the solution remaining at the bottom of the furnace to improve the fluidity of the solution. .
Still further, according to claim 6 of the present invention, after oxygen-enriched air is blown onto the solution, the solution is cooled and solidified, and the solidified solution is crushed and removed. Therefore, the solidified residual solution is The solidified solution is brittle and easy to be crushed because it is sufficiently oxidized and caramized. Therefore, the work of removing the solidified melt from the bottom of the furnace can be easily performed, and the damage to the hearth can be reliably prevented, and the hearth inspection, hearth dismantling, and transshipment work can be performed. It can be smoothly performed, and excellent effects such as a reduction in working time, a reduction in the number of workers, an improvement in the operating rate, and a reduction in the burden on workers can be achieved.

【図面の簡単な説明】[Brief description of drawings]

【図1】 銅の連続精錬装置の一例を示す説明図であ
る。
FIG. 1 is an explanatory diagram showing an example of a copper continuous refining apparatus.

【符号の説明】 C 粗銅 3 製銅炉 5b ランス 10 底抜き口[Explanation of symbols] C crude copper 3 Copper furnace 5b Lance 10 Bottom outlet

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 炉床煉瓦の点検あるいは解体、積替を行
う際に、炉底部に残留している溶体を除去する定置型製
銅炉における残留溶体の除去方法であって、上記溶体を
上記炉底部から抜き出すに際して、上記溶体の上方から
ランスによって酸素富化空気を吹き付け、上記残留溶体
の少なくとも一部をカラミ化することを特徴とする製銅
炉における残留溶体の除去方法。
1. A method for removing a residual solution in a stationary copper furnace for removing a solution remaining at the bottom of a furnace floor when inspecting, dismantling, or transshipping the brick, wherein the solution is When extracting from the bottom of the furnace, blow oxygen-enriched air from above the solution with a lance to remove the residual solution.
Method for removing residual solution in converting furnace, characterized that you Karami of at least part of the.
【請求項2】 ランス高さを溶体面から0.5〜2mに
設定したことを特徴とする請求項1記載の製銅炉におけ
る残留溶体の除去方法。
2. The method for removing a residual solution in a copper-making furnace according to claim 1, wherein the lance height is set to 0.5 to 2 m from the solution surface.
【請求項3】 ランスによって吹き付ける酸素富化空気
の酸素濃度を40〜70%に設定したことを特徴とする
請求項1または2記載の製銅炉における残留溶体の除去
方法。
3. The method for removing a residual solution in a copper-making furnace according to claim 1, wherein the oxygen concentration of the oxygen-enriched air blown by the lance is set to 40 to 70%.
【請求項4】 ランスによって吹き付ける酸素富化空気
の流速を130〜150Nm/sに設定したことを特徴
とする請求項1、2または3記載の製銅炉における残留
溶体の除去方法。
4. The method for removing residual solution in a copper-making furnace according to claim 1, 2 or 3, wherein the flow rate of the oxygen-enriched air blown by the lance is set to 130 to 150 Nm / s.
【請求項5】 炉底部から溶体を抜き出すに際して、バ
ーナーにより炉内部を加熱することを特徴とする請求項
1、2、3または4記載の製銅炉における残留溶体の除
去方法。
5. The method for removing a residual solution in a copper-making furnace according to claim 1, wherein the inside of the furnace is heated by a burner when the solution is extracted from the bottom of the furnace.
【請求項6】 酸素富化空気を溶体に吹き付けた後、こ
の溶体を冷却固化させて、この固化した溶体を破砕して
除去することを特徴とする請求項1、2、3、4または
5記載の製銅炉における残留溶体の除去方法。
6. The method of claim 1, wherein the oxygen-enriched air is blown onto the solution, and then the solution is cooled and solidified, and the solidified solution is crushed and removed. A method for removing a residual solution in a copper manufacturing furnace according to the description.
JP34978697A 1997-12-18 1997-12-18 Removal method of residual solution in copper making furnace Expired - Lifetime JP3528553B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34978697A JP3528553B2 (en) 1997-12-18 1997-12-18 Removal method of residual solution in copper making furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34978697A JP3528553B2 (en) 1997-12-18 1997-12-18 Removal method of residual solution in copper making furnace

Publications (2)

Publication Number Publication Date
JPH11181534A JPH11181534A (en) 1999-07-06
JP3528553B2 true JP3528553B2 (en) 2004-05-17

Family

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Country Link
JP (1) JP3528553B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101865603A (en) * 2010-06-07 2010-10-20 中国瑞林工程技术有限公司 A kind of charging method and equipment for anode refining furnace
CN106282597B (en) * 2016-08-19 2019-01-25 铜陵有色金属集团股份有限公司金冠铜业分公司 The application method of top blast furnace

Also Published As

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