JP2002275554A - Method for heat-insulating converter - Google Patents

Method for heat-insulating converter

Info

Publication number
JP2002275554A
JP2002275554A JP2001070901A JP2001070901A JP2002275554A JP 2002275554 A JP2002275554 A JP 2002275554A JP 2001070901 A JP2001070901 A JP 2001070901A JP 2001070901 A JP2001070901 A JP 2001070901A JP 2002275554 A JP2002275554 A JP 2002275554A
Authority
JP
Japan
Prior art keywords
converter
furnace
solid fuel
copper
lid
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
Application number
JP2001070901A
Other languages
Japanese (ja)
Inventor
Koji Noda
晃次 乃田
Takeshi Ochi
武 越智
Nobuyuki Furui
伸幸 古井
Akira Yamashita
山下  明
Kimihiro Shimokawa
公博 下川
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.)
Mitsui Mining and Smelting Co Ltd
Original Assignee
Mitsui Mining and Smelting 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 Mitsui Mining and Smelting Co Ltd filed Critical Mitsui Mining and Smelting Co Ltd
Priority to JP2001070901A priority Critical patent/JP2002275554A/en
Publication of JP2002275554A publication Critical patent/JP2002275554A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for heat-insulating a converter in which the converter can be favorably heat-insulated when the operation is stopped. SOLUTION: In this method, solid fuel is burned in the converter 1 when the operation is stopped, and/or flame 7 of liquid or gas fuel is blown from a tuyere 3 into the converter, and/or the tuyere 2 is covered by a converter lid 5.

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、転炉保温方法に関
する。
[0001] The present invention relates to a method for keeping a converter warm.

【0002】[0002]

【従来の技術】転炉を用いて銅湯を溶製する溶製操業に
おいては、自溶炉等のマット溶錬炉で産出した(Cu,Fe)S
を主成分とするマット(「かわ」ともいう;銅品位63〜
65%程度)とSiO2を主成分とする珪酸鉱を、図4に示す
ような例えばピアス・スミス型の周方向傾転可能な円筒
横型の転炉1の炉口2(原料等の装入および炉内反応生
成物等の抽出などのための通路穴。装入口または仕事口
ともいう。)から炉内に装入し、かつ炉体下部に配列さ
れたノズルからなる羽口3から空気または酸素富化空気
10を吹き込み、造かん期、次いで造銅期(製銅期ともい
う。)を経て、銅湯(「かね」ともいう;銅品位99%程
度)を溶製する。
2. Description of the Related Art In a smelting operation for melting copper hot water using a converter, (Cu, Fe) S produced in a mat smelting furnace such as a flash smelting furnace is used.
(Mainly referred to as “kawa”; copper grade 63 ~)
A silicate ore containing SiO2 as a main component and a pierce-smith type cylindrical horizontal converter 1 capable of tilting in the circumferential direction as shown in FIG. A passage hole for extracting reaction products and the like in the furnace. Also referred to as a charging port or a work port.) Air or oxygen is charged into the furnace through a tuyere 3 composed of nozzles arranged at the lower part of the furnace body. Enriched air
10 is blown in, and after a brewing period, and then a copper making period (also called a copper making period), a copper hot water (also called "kane"; copper grade of about 99%) is melted.

【0003】造かん期においては、主として、式(1) :
2(Cu,Fe)S +2O2+SiO2→Cu2S+2FeO・SiO2+SO2 の反
応が促進され、Cu2S主体の白かわの溶体と、2FeO・SiO2
主体のスラグ(「かん」または「からみ」ともいう)
と、亜硫酸ガス(SO2 )とが生成し、所定の反応が終わ
ったところで空気等の送風が止められる。白かわは炉内
に留置されて次工程の造銅期の原料になる。白かわより
も小比重で白かわ湯面上に浮くスラグは適宜転炉1を傾
転させて炉口2から炉外に排出される。操業中すなわち
送風中に発生する亜硫酸ガスは炉口2を覆うように設け
たフード4から炉外に排出され、その途中で顕熱を転炉
廃熱ボイラ30等に回収されながら硫酸工場に送られる。
なお、転炉1の傾転時にはフード4の前面可動フード4A
が引き上げられて炉口2が開放される。
[0003] In the period of irrigation, mainly the formula (1):
The reaction of 2 (Cu, Fe) S + 2O 2 + SiO 2 → Cu 2 S + 2FeO · SiO 2 + SO 2 is promoted, and a solution of white glue mainly composed of Cu 2 S and 2FeO · SiO 2
The main slag (also called "kan" or "karami")
Then, sulfur dioxide gas (SO 2 ) is generated, and when a predetermined reaction is completed, the blowing of air or the like is stopped. The white rice is kept in the furnace and becomes a raw material for the copper making stage of the next process. The slag floating on the surface of the white water with a specific gravity smaller than that of the white water is discharged from the furnace port 2 to the outside of the furnace by appropriately tilting the converter 1. Sulfurous acid gas generated during operation, i.e., during blowing, is discharged out of the furnace from a hood 4 provided to cover the furnace port 2, and sensible heat is sent to a sulfuric acid factory while being recovered by a converter waste heat boiler 30 and the like. Can be
When the converter 1 is tilted, the front movable hood 4A of the hood 4
Is lifted and the furnace port 2 is opened.

【0004】造銅期においては、主として、式(2) :Cu
2S+O2→Cu+SO2 の反応が促進され、実質的にCuからな
る銅湯Aと亜硫酸ガスとが生成する。なお、これ以外に
銅湯よりも高融点小比重のFe3O4 主体で銅分を含有する
残存物Bが少量生成し、銅湯面上に浮遊する。銅湯は造
銅期終了後にレードルを介して次工程の精製炉に移さ
れ、さらに高い銅品位(99.4%程度)の粗銅に精製され
る。残存物は、銅湯排出の際炉内に残し、新しく装入し
たマットに対する造かん期で処理される。亜硫酸ガスは
造かん期同様にフード4から排出される。
In the copper making period, mainly the formula (2): Cu
The reaction of 2 S + O 2 → Cu + SO 2 is promoted, and copper hot water A substantially composed of Cu and sulfurous acid gas are generated. In addition, a small amount of a residual B containing a copper component mainly composed of Fe 3 O 4 having a higher melting point and a lower specific gravity than the copper melt is generated and floats on the copper melt surface. After the end of the copper making period, the copper hot water is transferred to the refining furnace of the next process via a ladle to be refined into blister copper with a higher copper grade (about 99.4%). The remnants are left in the furnace when the copper melt is discharged, and are treated during the fermentation period for the newly charged mat. Sulfurous acid gas is discharged from the hood 4 in the same manner as during the period of making.

【0005】[0005]

【発明が解決しようとする課題】銅湯溶製用の転炉で
は、転炉工程およびその前後工程であるマット溶錬炉工
程、精製炉工程、硫酸製造工程等における操業調整およ
び設備トラブルならびにその修復工事等のため溶製(操
業)を中断する場合がある。操業中断が緊急で短時間の
場合、羽口からの酸素含有気体の供給が停止され、その
ままにしておくと、炉内の銅湯、マット等の溶体の温度
が適正反応温度未満に低下して操業再開に支障をきた
す。また、中断が長期間にわたる場合は、転炉廃熱ボイ
ラや硫酸工場等に支障がない限り、造銅期まで終えて銅
湯を転炉から排出し、炉内を空の状態にしておくが、そ
のままでは炉内温度低下のために次の造かん期において
スラグの生成反応がスムースに行われない等の支障をき
たす。また残存物が炉内レンガに固着して炉内容積が減
少することにもなる。
In a converter for smelting copper melt, operation adjustment and equipment troubles in a converter smelting furnace process, a refining furnace process, a sulfuric acid production process, etc., which are processes before and after the converter process, and troubles in the process. Melting (operation) may be interrupted due to restoration work. If the operation is interrupted for a short period of time, the supply of oxygen-containing gas from the tuyere is stopped, and if left as it is, the temperature of the solution such as copper bath and mat in the furnace falls below the appropriate reaction temperature. This will hinder restarting operations. Also, if the interruption is for a long period of time, unless the converter waste heat boiler or sulfuric acid plant has any problems, the copper melt is discharged from the converter after the copper making period, and the furnace is left empty. However, as it is, the reaction in the slag is not smoothly performed in the next fermentation period due to a decrease in the furnace temperature. Further, the residue adheres to the bricks in the furnace, and the volume in the furnace is reduced.

【0006】そこで、休風中の転炉において、マット、
銅湯等の溶体の出し入れ期間を除く転炉操業の中断中に
羽口からバーナーを用いて灯油等の液体あるいはガス燃
料火炎を吹き込んで空になった炉内あるいは残留する溶
体を保温することが行われている。この液体あるいはガ
ス燃料火炎吹き込みによる転炉保温方法は有効である
が、長時間にわたる保温の場合には、・炉内温度の低下
が避けられない、・炉内に溶体がある場合、 羽口への溶
体の逆流防止のため羽口位置を高くしなければならず、
羽口へのバーナのセットは作業の安全上好ましくない、
という問題があった。
[0006] Therefore, in the converter during the cold wind, the mat,
During the operation of the converter excluding the period of taking in and out the solution such as copper hot water, it is possible to use a burner to blow liquid or gas fuel flame such as kerosene from the tuyere through the tuyere to keep the inside of the furnace empty or the remaining solution. Is being done. This method of insulating the converter by injecting a liquid or gaseous fuel flame is effective, but in the case of long-term heat insulation, a decrease in the furnace temperature is unavoidable. The tuyere position must be raised to prevent backflow of the solution
Setting the burner to the tuyere is not preferable for work safety,
There was a problem.

【0007】そこで、本発明は、比較的長時間の操業中
断時の転炉保温をより有利に行いうる転炉保温方法を提
供することを目的とする。
Accordingly, an object of the present invention is to provide a converter insulation method capable of more advantageously maintaining the converter insulation during a relatively long operation interruption.

【0008】[0008]

【課題を解決するための手段】前記目的は、以下の点を
要旨とする本発明によって達成された。 (1)転炉を用いて銅湯を溶製する操業の中断時に転炉
内で固体燃料を燃焼させることを特徴とする転炉保温方
法。 (2)転炉を用いて銅湯を溶製する操業の中断時に転炉
内で固体燃料を燃焼させるとともに羽口から転炉内に液
体あるいはガス燃料火炎を吹き込むことを特徴とする転
炉保温方法。
The above object has been attained by the present invention having the following points. (1) A method for keeping a converter warm, comprising burning solid fuel in the converter when the operation of melting copper hot water using the converter is interrupted. (2) Insulation of the converter characterized by burning solid fuel in the converter and blowing liquid or gas fuel flame from the tuyere into the converter when the operation of melting copper hot water using the converter is interrupted. Method.

【0009】(3)転炉を用いて銅湯を溶製する操業の
中断時に転炉内で固体燃料を燃焼させるとともに転炉の
炉口を炉蓋で覆うことを特徴とする転炉保温方法。 (4)転炉を用いて銅湯を溶製する操業の中断時に転炉
内で固体燃料を燃焼させるとともに羽口から転炉内に液
体あるいはガス燃料火炎を吹き込み、かつ転炉の炉口を
炉蓋で覆うことを特徴とする転炉保温方法。
(3) A method for keeping a converter warm, characterized by burning solid fuel in the converter when the operation of melting the copper melt using the converter is interrupted and covering the furnace opening of the converter with a furnace lid. . (4) When the operation of melting copper hot water using the converter is interrupted, solid fuel is burned in the converter while liquid or gas fuel flame is blown into the converter from the tuyere, and the furnace outlet of the converter is closed. A converter insulation method comprising covering with a furnace lid.

【0010】[0010]

【発明の実施の形態】本発明では、操業の中断時に転炉
内で固体燃料(薪等の木材を除く)を燃焼させ、あるい
はさらに羽口から転炉内に液体あるいはガス燃料火炎を
吹き込む方法、または、操業の中断時に固体燃料を燃焼
させるとともに羽口から転炉内に液体あるいはガス燃料
火炎を吹き込み、かつ転炉の炉口を炉蓋で覆う方法がと
られる。
DETAILED DESCRIPTION OF THE INVENTION In the present invention, a method of burning solid fuel (excluding wood such as firewood) in a converter when operation is interrupted, or blowing liquid or gaseous fuel flame into the converter from tuyeres. Alternatively, when the operation is interrupted, the solid fuel is burned, a liquid or gas fuel flame is blown into the converter from the tuyere, and the furnace opening of the converter is covered with a furnace lid.

【0011】コークスや石炭等の炭素を主成分とする固
体燃料を転炉内に装入するとこれらは、炉内に溶体があ
ればその表面を浮遊して覆い、また炉内に溶体が無い場
合でも炉内中央付近の耐火物表面を覆って炉口からの熱
放散を防止するとともに該表面を加熱して、炉内溶体あ
るいは炉内耐火物の温度低下を防止する。固体燃料とし
ては、 水分が15質量%以下のコークスあるいは石炭が、
炉内での水蒸気爆発の危険性がなく取扱いが容易で、し
かも安価であり、好ましい。
When a solid fuel containing carbon as a main component, such as coke or coal, is charged into a converter, the converter floats and covers the surface of the furnace if there is a solution. However, the surface of the refractory near the center of the furnace is covered to prevent heat dissipation from the furnace port and to heat the surface to prevent the temperature of the furnace melt or the refractory inside the furnace. Coke or coal with a water content of 15% by mass or less is used as a solid fuel.
It is preferable because there is no danger of steam explosion in the furnace and it is easy to handle and inexpensive.

【0012】これらの固体燃料は、珪酸鉱等を炉内に装
入するシュート等を利用して炉口から装入してもよい
し、あるいは装入ボートに積載し、天井クレーンを用い
て炉口から全量を一度に炉内に装入してもよい。また羽
口から微粉状の固体燃料を吹き込むことも可能である。
固体燃料は液体あるいはガス燃料に比較して燃焼速度が
遅いので、転炉操業の中断状態が1時間以上、特に3時
間以上続く場合に使用するのが好ましい。固体燃料の使
用にあたっては、中断時間内に燃え尽きるように装入量
を調整することが肝要である。というのは、固体燃料は
比重が小さいために炉内に多量の固体燃料が残ったまま
送風を開始すると赤熱した未燃焼固体燃料が炉外に吹き
出し、 転炉周辺設備の火災の原因となったり、 転炉廃熱
ボイラ内等の煙灰に着火して操業の支障となる等の問題
を引き起こすからである。例えば発熱量約8500kcal/k
g、揮発分9〜12%、灰分0.1 〜0.3 %、水分8%のオ
イルコークス500 kgを炉内に装入した場合、燃え尽きる
のに約5〜10時間かかる。
[0012] These solid fuels may be charged from the furnace port using a chute or the like for charging silicate ore or the like into the furnace, or may be loaded on a charging boat and used for the furnace using an overhead crane. The whole amount may be charged into the furnace at one time from the mouth. It is also possible to blow fine powdery solid fuel from the tuyere.
Since the solid fuel has a lower combustion rate than the liquid or gas fuel, it is preferably used when the operation of the converter is interrupted for 1 hour or more, particularly 3 hours or more. When using solid fuel, it is important to adjust the charge so that it burns out during the suspension time. This is because solid fuel has a low specific gravity, so if a large amount of solid fuel is left inside the furnace and air is blown, red-hot unburned solid fuel will blow out of the furnace and cause fires around the converter. This is because the smoke in the converter waste heat boiler may ignite and cause problems such as hindrance to the operation. For example, calorific value about 8500kcal / k
When 500 kg of oil coke containing g, 9 to 12% of volatile matter, 0.1 to 0.3% of ash, and 8% of water is charged into the furnace, it takes about 5 to 10 hours to burn out.

【0013】これらの固体燃料の粒径は、炉口から装入
する場合、あまり細かいと炉口からの上昇気流により装
入時に炉外へ飛散する割合が多くなるので、篩分けして
粒径0.5mm 以上の質量比率が90%以上の固体燃料を使う
ことが好ましい。さらに好ましくは、篩分けして粒径3
〜70mmの範囲にある固体燃料の割合が質量比率で90%以
上であるものがよい。粒径が100mm を超えると溶体等の
被覆効果が低下し、 燃焼速度もさらに遅くなり好ましく
ない。
When the solid fuel is charged from the furnace port, if the particle diameter is too small, the proportion of the solid fuel scattered outside the furnace at the time of charging due to the rising air current from the furnace port increases. It is preferable to use a solid fuel having a mass ratio of 0.5 mm or more and 90% or more. More preferably, it is sieved to a particle size of 3
It is preferable that the proportion of the solid fuel in the range of up to 70 mm is 90% or more by mass. If the particle size exceeds 100 mm, the effect of coating the solution or the like is reduced, and the burning rate is further decreased, which is not preferable.

【0014】なお、羽口からのバーナを用いた3mm未満
の微粉炭等の吹き込みは、その燃焼速度が遅いために炉
内で完全燃焼せず、炉外に出てアフタバーンする割合が
多くなる。また、 固体燃料は、前述のように燃焼速度が
遅いため、 保温効果を上げるためには同時に羽口から液
体あるいはガス燃料の火炎を吹き込むことが好ましい。
[0014] Injection of pulverized coal of less than 3 mm from the tuyere using a burner does not completely burn in the furnace due to its slow burning rate, and increases the rate of afterburning out of the furnace. Further, since the solid fuel has a low burning rate as described above, it is preferable to simultaneously blow a liquid or gaseous fuel flame from the tuyere in order to increase the heat retaining effect.

【0015】この保温効果をさらに確実なものにするた
めには、炉口に炉蓋を被せることが好ましい。この炉蓋
被着により炉口からの熱放散が有効に抑制されて炉内保
温力が増強される。前記液体燃料としては、取り扱い性
がよく、炉蓋をしても燃焼効率のよい灯油、A重油等が
好ましく用いうる。また、前記ガス燃料としては、液体
燃料と同じく取り扱い性がよく、燃焼効率のよい液化石
油ガス、プロパン、ブタン、プロパンとブタンの混合ガ
ス、アンモニアガス等が好ましく用いうる。
In order to further ensure the heat retaining effect, it is preferable to cover the furnace port with a furnace lid. Due to the attachment of the furnace lid, heat dissipation from the furnace port is effectively suppressed, and the insulative power in the furnace is enhanced. As the liquid fuel, kerosene, fuel oil A, or the like, which has good handleability and has high combustion efficiency even with a furnace lid, can be preferably used. In addition, as the gaseous fuel, liquefied petroleum gas, propane, butane, a mixed gas of propane and butane, ammonia gas, and the like, which have good handleability and good combustion efficiency like liquid fuel, can be preferably used.

【0016】なお、炉修後の転炉内で固体燃料を燃焼さ
せるとともに炉口を炉蓋で覆って、転炉内の耐火物を効
率的に加熱・ 昇温することもできる。また、炉修後の転
炉内で固体燃料および、 液体燃料あるいは ガス燃料の
うちの少なくとも一つを燃焼させるとともに炉口を炉蓋
で覆って、転炉内の耐火物を効率的に加熱・ 昇温するこ
ともできる。
The refractory in the converter can be efficiently heated and heated by burning the solid fuel in the converter after the furnace repair and covering the furnace opening with a furnace lid. In addition, at least one of the solid fuel, liquid fuel, and gas fuel is burned in the converter after the furnace repair, and the furnace opening is covered with a furnace lid to efficiently heat the refractory in the converter. The temperature can be raised.

【0017】炉蓋は、炉口の開口部全体を被覆可能な寸
法のものが好ましく、その形状は特に限定されないが、
製作容易性や着脱容易性などの観点から可及的単純な形
状、例えば図3に示すような、転炉の外面形状に倣う内
面形状を有する円筒壁の一部を切り取ったような形状が
望ましい。また、炉蓋5は、強度、耐熱性などの観点か
ら、鋼材と耐火物との複合体で形成されるのが好まし
く、例えば図3のような、鋼製枠5A内に不定形耐火物5B
を施工して形成したものが好適である。鋼製枠5A内には
不定形耐火物5Bを支持するためのアンカーが設けられて
いるのが好ましい。炉蓋5は不定形耐火物5Bを炉内側に
向かせて炉口2に設置する。また、炉蓋5は適宜図3に
示すような装着位置ずれあるいは転炉傾転時の炉口から
の外れ防止用の支柱51や燃焼排ガス逃がし用の排煙口52
を設けたものが好ましい。かかる支柱を有する炉蓋であ
れば、例えば転炉内に溶体が入っている場合において、
炉口面が水平より大きく傾いていても、これを炉口に被
せたまま転炉を傾転させることができ、操業の自由度を
損なうことがない。
The furnace lid is preferably of a size capable of covering the entire opening of the furnace port, and its shape is not particularly limited.
A shape as simple as possible from the viewpoint of ease of production and ease of attachment / detachment, for example, a shape obtained by cutting off a part of a cylindrical wall having an inner surface shape following the outer shape of the converter as shown in FIG. 3 is desirable. . Further, the furnace lid 5 is preferably formed of a composite of a steel material and a refractory from the viewpoints of strength, heat resistance and the like. For example, as shown in FIG.
What is formed by constructing is preferred. It is preferable that an anchor for supporting the irregular-shaped refractory 5B is provided in the steel frame 5A. The furnace lid 5 is installed at the furnace opening 2 with the irregular-shaped refractory 5B facing the inside of the furnace. The furnace lid 5 is appropriately provided with a support column 51 for preventing the mounting position from being displaced from the furnace port when the converter is tilted or the converter is tilted as shown in FIG.
Is preferably provided. In the case of a furnace lid having such columns, for example, when a solution is contained in a converter,
Even if the furnace port surface is inclined more than horizontal, the converter can be tilted while covering the furnace port, and the degree of freedom of operation is not impaired.

【0018】前記炉蓋の炉口への着脱は、天井クレーン
を用いて行うことも可能ではあるが、汎用であるため緊
急の場合に即座の使用が難しい場合がある。また、天井
クレーンで吊った炉蓋は炉口との位置合わせが困難で天
井クレーン運転手に大きな負担がかかる。このような難
点があるので、別途専用の着脱装置を用いることが好ま
しい。かかる着脱装置としては、例えば図1〜図2に示
すようなもの、すなわち、銅湯溶製用転炉1の炉口2に
着脱可能に被さる炉蓋5と、該炉蓋5を昇降可能に保持
して定位置の炉口2に着脱する炉蓋着脱機6とを有する
転炉炉蓋装置が好適である。この装置によれば炉蓋の着
脱を自動化できて、天井クレーン運転手の負担等を軽減
することができる。
The furnace lid can be attached to and detached from the furnace port using an overhead crane. However, since it is a general purpose, it may be difficult to use it immediately in an emergency. Further, it is difficult to position the furnace lid suspended by the overhead crane with the furnace opening, which places a heavy burden on the overhead crane operator. Because of these difficulties, it is preferable to use a dedicated attachment / detachment device separately. For example, as shown in FIG. 1 to FIG. 2, a furnace lid 5 that detachably covers the furnace port 2 of the converter 1 for melting copper hot water, and the furnace lid 5 that can be moved up and down. A converter furnace cover device having a furnace cover attaching / detaching machine 6 which is held and attached to and detached from the furnace port 2 at a fixed position is preferable. According to this device, the attachment and detachment of the furnace lid can be automated, and the burden on the overhead crane operator and the like can be reduced.

【0019】本例の炉蓋着脱機6は、炉蓋5を吊持する
ワイヤ6Dと、該ワイヤ6Dを案内する滑車6Cと、前記ワイ
ヤ6Dを繰り出しあるいは繰り入れる繰入出機6Bと、前記
滑車6Cおよび前記繰入出機6Bを支持するアーム6Aと、該
アーム6Aを支持して定位置の炉口2直上位置からその斜
め上方の待機位置までの間を90°回転させる回転支軸6E
とを有する。なお、繰入出機6Bの繰入出動作と回転支軸
6Eのアーム6A回転動作とはそれぞれモータ(図示省略)
で駆動され、該モータはボタン操作により運転される。
The furnace lid attaching / detaching machine 6 of this embodiment includes a wire 6D for suspending the furnace lid 5, a pulley 6C for guiding the wire 6D, a feeding / unloading machine 6B for feeding or feeding the wire 6D, and the pulley 6C. And an arm 6A for supporting the feeding / unloading machine 6B, and a rotary support shaft 6E for supporting the arm 6A and rotating by 90 ° from a position immediately above the furnace port 2 at a fixed position to a standby position obliquely above the furnace port 2.
And The feeding and unloading operation of the feeding and unloading machine 6B and the rotating spindle
6E arm 6A rotation operation is a motor (not shown)
, And the motor is operated by button operation.

【0020】この転炉炉蓋装置6は例えば以下のように
運転される。 1)操業中断(あるいは停止)時に前面可動フード4が
退いた後、保温時間に応じて、天井クレーンを用いてコ
ークスを炉口から炉内に装入する。 2)炉蓋をするための定位置にくるように転炉の傾転角
度を調整する。通常、定位置の炉口の面と地面とのなす
角度が水平ないし炉口の面が溶体排出側(反羽口側)に
約50°傾いた角度の間から選択される所定の位置であ
る。なお、炉口が定位置より前後に例えば15°程度角度
がずれていても炉蓋は被せることができる。
The converter furnace cover device 6 is operated, for example, as follows. 1) After the front movable hood 4 retreats when the operation is interrupted (or stopped), coke is charged into the furnace from the furnace port using an overhead crane according to the heat retention time. 2) Adjust the tilt angle of the converter so that it comes to a fixed position for closing the furnace. Normally, the angle formed between the surface of the furnace port at the fixed position and the ground is a predetermined position selected from a horizontal angle or an angle at which the surface of the furnace port is inclined by about 50 ° toward the solution discharge side (the counter tuyere side). . The furnace lid can be covered even if the furnace port is shifted from the home position back and forth by, for example, about 15 °.

【0021】3)アーム6Aを下方に90°回転させて水平
になる位置に倒す。これにより炉蓋5が転炉1の斜め上
方の待機位置から定位置の炉口2の鉛直上方の位置に運
ばれる。炉蓋5の姿勢は水平であっても多少傾いていて
もよい。炉蓋と炉口の面とが平行の関係になくても、ワ
イヤを弛ませれば、炉蓋は炉口に被さるからである。 4)ワイヤ6Dを繰り出す。これにより炉蓋5が下降して
炉口2に被さる。
3) The arm 6A is turned downward by 90 ° and lowered to a horizontal position. As a result, the furnace lid 5 is carried from the standby position obliquely above the converter 1 to a position vertically above the furnace port 2 at a fixed position. The attitude of the furnace lid 5 may be horizontal or slightly inclined. This is because, even if the furnace lid and the surface of the furnace port are not in a parallel relationship, if the wire is loosened, the furnace cover covers the furnace port. 4) Pay out the wire 6D. This lowers the furnace lid 5 and covers the furnace port 2.

【0022】5)炉内に溶体が無い場合には、バーナを
羽口から差し込み易い角度に転炉を傾転させる。操業中
断中はこの状態を保つ。なお、燃焼排ガスは、排煙口52
から排出される。 6)操業再開前に転炉を傾転させて炉口を所定の定位置
に戻し、ワイヤ6Dを繰り入れて炉蓋5を上昇させアーム
6Aに引き寄せて固定する。
5) When there is no solution in the furnace, the converter is tilted to an angle at which the burner can be easily inserted from the tuyere. This state is maintained during operation interruption. The flue gas is discharged from the exhaust
Is discharged from. 6) Before restarting the operation, the converter is tilted to return the furnace port to a predetermined home position, the wire 6D is inserted, the furnace cover 5 is raised, and the arm is raised.
Pull to 6A and fix.

【0023】7)アーム6Aを上方に90°回転させて炉蓋
5を待機位置に戻す。このように、本発明の転炉炉蓋装
置によれば、炉口への炉蓋着脱作業を極めて容易に行う
ことができる。ところで、本例ではアームの回転角度を
90°とし、また、回転方向を上下方向(鉛直面内での回
転)としたが、本発明はこれに限られず、回転の角度や
方向などは場合場合に応じて適宜に設定すればよい。
7) Rotate the arm 6A upward by 90 ° to return the furnace lid 5 to the standby position. As described above, according to the converter furnace cover device of the present invention, the work of attaching and detaching the furnace cover to the furnace port can be performed extremely easily. By the way, in this example, the rotation angle of the arm is
Although the rotation direction is set to 90 ° and the rotation direction is set to the vertical direction (rotation in the vertical plane), the present invention is not limited to this, and the rotation angle and direction may be set appropriately according to the case.

【0024】なお、回転方向が上下方向の場合、回転角
度は60〜120 °の範囲がよい。回転角度が60°より小さ
いと、マットを炉口から炉内に装入するレードルと干渉
するので好ましくなく、一方、120 °より大きいと、炉
蓋を被せるまでに時間がかかりすぎ、また公害対策とし
て設置されている亜硫酸ガスの漏れをシールするフード
の側面と干渉するので、好ましくない。
When the rotation direction is the vertical direction, the rotation angle is preferably in the range of 60 to 120 °. If the rotation angle is less than 60 °, the mat interferes with the ladle to be charged into the furnace from the furnace port, which is not preferable.On the other hand, if the rotation angle is more than 120 °, it takes too much time to cover the furnace lid, and measures against pollution are required. It is not preferable because it interferes with the side surface of the hood that seals the leakage of sulfurous acid gas installed.

【0025】また、炉内に溶体が入っている場合、羽口
が溶体に浸らないように炉口が定位置より溶体排出側
(反羽口側)にずれた位置で保温することもあるが、こ
の場合は、図2に示すように炉蓋5の羽口側に付けた支
柱51により安定して炉口2に炉蓋5を装着することがで
きる。
When a solution is contained in the furnace, the temperature may be kept at a position where the furnace port is shifted from a fixed position to a solution discharge side (opposite the tuyere side) so that the tuyere is not immersed in the solution. In this case, as shown in FIG. 2, the column 51 attached to the tuyere side of the furnace lid 5 allows the furnace lid 2 to be stably mounted on the furnace port 2.

【0026】[0026]

【実施例】(実施例1) 銅湯生産量210 トン/ロット
の転炉での第1造かん操業中、冷材装入後に他工程のト
ラブルにより3時間の操業中断を余儀なくされた。そこ
で本発明に従い、発熱量8500kcal/kg 、水分8%、粒度
については粒径10〜30mmの範囲にある質量比率が100 %
であるオイルコークス300kg (3時間でほぼ燃え尽きる
量)をボートで天井クレーンを用いて炉口から炉内に全
量を一度に装入し、かつ、操業中断中ずっと羽口から灯
油50l/h ×バーナ2本の炉内吹き込みを続けることによ
り、コークスの炉内溶体被覆および燃焼熱、ならびに灯
油の燃焼熱による転炉内保温を実施した。
EXAMPLES (Example 1) During the first canning operation in a converter with a production volume of 210 tons / lot of copper hot water, a trouble in another process after charging the cold material forced an interruption of the operation for 3 hours. Therefore, according to the present invention, the calorific value is 8500 kcal / kg, the water content is 8%, and the particle size is 10% to 30mm.
300 kg of oil coke (amount that almost burns out in 3 hours) is charged all at once from the furnace mouth to the furnace by a boat using an overhead crane, and kerosene is 50 l / h from the tuyere while the operation is suspended. By continuously blowing the two furnaces, the coke in-furnace solution coating and combustion heat of coke and the heat retention in the converter by the combustion heat of kerosene were performed.

【0027】その結果、操業再開後において特にトラブ
ルなく造かん期操業を行うことができ、スラグの流動性
についても特に問題はなかった。 (実施例2) 銅湯生産量210 トン/ロットの転炉での
造銅期操業後、他工程のトラブルにより7時間の操業中
断を余儀なくされた。そこで本発明に従い、銅湯をレー
ドルに排出後に、粒径10〜25mmの範囲にある質量比率が
100 %であるオイルコークス500kg (7時間でほぼ燃え
尽きる量)をボートで天井クレーンを用いて炉口から炉
内に一度に装入し、炉蓋をし、かつ、操業中断中ずっと
羽口から灯油45l/h ×バーナ2本の炉内吹き込みを続け
ることにより、コークスの耐火物被覆および燃焼熱、な
らびに灯油の燃焼熱による転炉内保温を実施した。
As a result, it was possible to carry out the slag making operation without any trouble after the restart of the operation, and there was no particular problem with the slag fluidity. (Example 2) After the copper making operation in a converter with a production volume of 210 tons / lot of copper hot water, a trouble in another process forced the interruption of the operation for 7 hours. Therefore, according to the present invention, after the copper melt is discharged to the ladle, the mass ratio in the range of particle diameter 10 to 25 mm
500 kg of 100% oil coke (amount almost burned out in 7 hours) was loaded into the furnace at once from the furnace port using a ceiling crane by a boat, the furnace lid was closed, and kerosene was supplied from the tuyere while the operation was suspended. By continuing to blow the inside of the furnace with two 45 l / h burners, the refractory coating of coke and the combustion heat, and the heat retention in the converter by the combustion heat of kerosene were carried out.

【0028】炉蓋による保温は図1〜図3に示した態様
で実施した。なお、この転炉の炉口開口寸法は、炉周方
向幅=2000mm、炉長方向幅=2700mmであったので、炉蓋
の外形寸法は、炉口開口部を余裕を持って被覆できるよ
うに、炉周方向幅=2540mm、炉長方向幅=2800mmとし、
また、厚さは200 mmとした。炉蓋の不定形耐火物には、
ヨータイ株式会社製のヨータイキャスコC-140-SC30を使
用した。なお、炉蓋には75mmφ×300mm 長さの支柱2本
と250mm 角の排煙口2孔を設けた。炉蓋着脱機について
は、アームおよび回転支柱を鋼材で製作し、繰入出機に
は通常のドラム巻取型のものを用いた。
The heat retention by the furnace lid was carried out in the manner shown in FIGS. The furnace opening size of this converter was furnace width in the circumferential direction = 2000 mm and furnace length direction width = 2700 mm, so that the outer dimensions of the furnace lid were designed so that the furnace opening could be covered with a margin. , Furnace width in the circumferential direction = 2540 mm, furnace width in the length direction = 2800 mm,
The thickness was 200 mm. For the refractory of the furnace lid,
Yotai Casco C-140-SC30 manufactured by Yotai Corporation was used. The furnace lid was provided with two columns of 75mmφ × 300mm length and two 250mm square exhaust holes. Regarding the furnace lid attaching / detaching machine, the arm and the rotating column were made of steel, and a normal drum winding type was used as the feeding / unloading machine.

【0029】その結果、冷材量を減量調整しなくても次
バッチの造かん期操業を行うことができた。
As a result, the operation for the next batch in the period of making could be performed without adjusting the amount of the cooling material.

【0030】[0030]

【発明の効果】本発明によれば、転炉操業中断時、長時
間保温ニーズに対して固体燃料が転炉内の溶体あるいは
耐火物を覆うとともに加熱するため保温効果が高まり、
加えて転炉の炉口に炉蓋を設置することによりさらに保
温効果が高まり、再開後の操業条件変更を要さず常に安
定した転炉操業を行うことができるようになり、また、
残存物の炉内レンガへの固着を防止でき、炉内容積がほ
ぼ一定に保たれるという種々格段の効果を奏する。
According to the present invention, when the operation of the converter is interrupted, the solid fuel covers and heats the solution or refractory in the converter in response to long-term heat-retaining needs, thereby increasing the heat-retaining effect.
In addition, by installing a furnace lid at the furnace opening of the converter, the heat retention effect is further enhanced, and it becomes possible to always perform a stable converter operation without changing the operating conditions after restarting,
The remnants can be prevented from sticking to the bricks in the furnace, and various effects can be obtained in that the furnace volume can be kept substantially constant.

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

【図1】転炉炉蓋装置の概要を示す正面図である。FIG. 1 is a front view showing an outline of a converter furnace cover device.

【図2】図1のAA矢視図である。FIG. 2 is a view taken in the direction of arrows AA in FIG. 1;

【図3】炉蓋の一例を示す立体図である。FIG. 3 is a three-dimensional view showing an example of a furnace lid.

【図4】一般的な転炉銅溶製方法の説明図である。FIG. 4 is an explanatory view of a general converter copper melting method.

【符号の説明】[Explanation of symbols]

1 転炉 2 炉口 3 羽口 4 フード 4A 前面可動フード 4B 後面可動板 5 炉蓋 5A 鋼製枠 5B 不定形耐火物 6 炉蓋着脱機 6A アーム 6B 繰入出機 6C 滑車 6D ワイヤ 6E 回転支軸 7 液体あるいはガス燃料火炎(例:灯油火炎) 10 空気または酸素富化空気 30 転炉廃熱ボイラ 51 支柱 52 排煙口 DESCRIPTION OF SYMBOLS 1 Converter 2 Furnace port 3 Tuyere 4 Hood 4A Front movable hood 4B Rear movable plate 5 Furnace lid 5A Steel frame 5B Irregular refractory 6 Furnace lid attaching / detaching machine 6A Arm 6B Feeding / unloading machine 6C Pulley 6D Wire 6E Rotating spindle 7 Liquid or gas fuel flame (eg kerosene flame) 10 Air or oxygen-enriched air 30 Converter waste heat boiler 51 Prop 52 Smoke outlet

フロントページの続き (72)発明者 古井 伸幸 岡山県玉野市日比6−1−1 三井金属鉱 業株式会社日比製煉所内 (72)発明者 山下 明 岡山県玉野市日比6−1−1 三井金属鉱 業株式会社日比製煉所内 (72)発明者 下川 公博 岡山県玉野市日比6−1−1 三井金属鉱 業株式会社日比製煉所内 Fターム(参考) 4K001 AA09 BA10 DA03 GA06 4K070 DA01 Continued on the front page (72) Inventor Nobuyuki Furui 6-1-1 Hibi, Tamano-shi, Okayama Pref. Mitsui Kinzoku Mining Co., Ltd. Hibiki Refinery (72) Inventor Akira Yamashita 6-1-1 Hibi, Tamano-shi, Okayama Pref. 1 Mitsui Mining & Smelting Co., Ltd. Hibiki Refinery (72) Inventor Kimihiro Shimokawa 6-1-1 Hibi, Tamano-shi, Okayama Pref. GA06 4K070 DA01

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 転炉を用いて銅湯を溶製する操業の中断
時に転炉内で固体燃料を燃焼させることを特徴とする転
炉保温方法。
1. A method for keeping a converter warm, wherein solid fuel is burned in the converter when the operation of melting the copper melt using the converter is interrupted.
【請求項2】 転炉を用いて銅湯を溶製する操業の中断
時に転炉内で固体燃料を燃焼させるとともに羽口から転
炉内に液体あるいはガス燃料火炎を吹き込むことを特徴
とする転炉保温方法。
2. A converter characterized by burning solid fuel in a converter and blowing a liquid or gas fuel flame from a tuyere into the converter when the operation of melting copper melt using a converter is interrupted. Furnace insulation method.
【請求項3】 転炉を用いて銅湯を溶製する操業の中断
時に転炉内で固体燃料を燃焼させるとともに転炉の炉口
を炉蓋で覆うことを特徴とする転炉保温方法。
3. A method for keeping a converter warm, comprising: burning solid fuel in the converter when the operation of melting the copper melt using the converter is interrupted; and covering a furnace opening of the converter with a furnace lid.
【請求項4】 転炉を用いて銅湯を溶製する操業の中断
時に転炉内で固体燃料を燃焼させるとともに羽口から転
炉内に液体あるいはガス燃料火炎を吹き込み、かつ転炉
の炉口を炉蓋で覆うことを特徴とする転炉保温方法。
4. When the operation of melting copper hot water using a converter is interrupted, solid fuel is burned in the converter and a liquid or gas fuel flame is blown into the converter from tuyeres. A converter insulation method comprising covering a mouth with a furnace lid.
JP2001070901A 2001-03-13 2001-03-13 Method for heat-insulating converter Pending JP2002275554A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001070901A JP2002275554A (en) 2001-03-13 2001-03-13 Method for heat-insulating converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001070901A JP2002275554A (en) 2001-03-13 2001-03-13 Method for heat-insulating converter

Publications (1)

Publication Number Publication Date
JP2002275554A true JP2002275554A (en) 2002-09-25

Family

ID=18928686

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2002275554A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007532771A (en) * 2004-04-07 2007-11-15 オースメルト リミテッド Process for converting copper
JP2017165994A (en) * 2016-03-14 2017-09-21 パンパシフィック・カッパー株式会社 Back surface hood of converter and opening and closing method thereof
CN115109886A (en) * 2022-07-11 2022-09-27 广东韶钢松山股份有限公司 Heat preservation method for long-time shutdown of converter

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5842156U (en) * 1981-09-14 1983-03-19 住友金属鉱山株式会社 Heat retention device for converter for nonferrous smelting
JPH0995744A (en) * 1995-09-29 1997-04-08 Sumitomo Metal Mining Co Ltd Horizontal type converter for copper smelting
JP2000199019A (en) * 1999-01-06 2000-07-18 Mitsui Mining & Smelting Co Ltd Method for holding and raising temperature of copper flash smelting furnace

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5842156U (en) * 1981-09-14 1983-03-19 住友金属鉱山株式会社 Heat retention device for converter for nonferrous smelting
JPH0995744A (en) * 1995-09-29 1997-04-08 Sumitomo Metal Mining Co Ltd Horizontal type converter for copper smelting
JP2000199019A (en) * 1999-01-06 2000-07-18 Mitsui Mining & Smelting Co Ltd Method for holding and raising temperature of copper flash smelting furnace

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007532771A (en) * 2004-04-07 2007-11-15 オースメルト リミテッド Process for converting copper
KR101241999B1 (en) 2004-04-07 2013-03-11 오토텍 오와이제이 Process for copper converting
USRE44850E1 (en) 2004-04-07 2014-04-22 Outotec Oyj Process for copper converting
JP2017165994A (en) * 2016-03-14 2017-09-21 パンパシフィック・カッパー株式会社 Back surface hood of converter and opening and closing method thereof
CN115109886A (en) * 2022-07-11 2022-09-27 广东韶钢松山股份有限公司 Heat preservation method for long-time shutdown of converter
CN115109886B (en) * 2022-07-11 2023-10-20 广东韶钢松山股份有限公司 Heat preservation method for long-time shutdown of converter

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