JPH0469575B2 - - Google Patents

Info

Publication number
JPH0469575B2
JPH0469575B2 JP23448486A JP23448486A JPH0469575B2 JP H0469575 B2 JPH0469575 B2 JP H0469575B2 JP 23448486 A JP23448486 A JP 23448486A JP 23448486 A JP23448486 A JP 23448486A JP H0469575 B2 JPH0469575 B2 JP H0469575B2
Authority
JP
Japan
Prior art keywords
furnace
inert gas
gas
melt
lance tube
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
JP23448486A
Other languages
Japanese (ja)
Other versions
JPS6389439A (en
Inventor
Takashi Yumura
Akio Ihara
Hidetoki Noguchi
Shigenori Masunaga
Yoshinobu Oda
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.)
Shin Etsu Chemical Co Ltd
Nippon Steel Corp
Original Assignee
Shin Etsu Chemical Co Ltd
Nippon Steel 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 Shin Etsu Chemical Co Ltd, Nippon Steel Corp filed Critical Shin Etsu Chemical Co Ltd
Priority to JP23448486A priority Critical patent/JPS6389439A/en
Publication of JPS6389439A publication Critical patent/JPS6389439A/en
Publication of JPH0469575B2 publication Critical patent/JPH0469575B2/ja
Granted legal-status Critical Current

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  • Manufacture, Treatment Of Glass Fibers (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はロツクウール原料である高炉溶融スラ
グを加熱する電気炉内に成分調整材を添加する方
法およびその装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method and an apparatus for adding a component adjusting material into an electric furnace for heating blast furnace molten slag, which is a raw material for rock wool.

〔従来の技術〕[Conventional technology]

ミネラルウール、スラグウール、ロツクウール
等の名称で呼ばれる無機繊維は天然岩石を溶解し
製綿しても製造されているが、我が国において最
も一般的には高炉スラグ砕石に必要に応じて成分
調整材を添加して電気炉、キユポラ等の溶融炉で
再溶融し、溶融物を製綿機に供給し遠心力及び/
又は圧力空気、スチーム等の流体圧力で繊維化す
る方法が採られている。この従来方法はスラグ砕
石を使用するので原料の輸送や貯蔵に便利であ
り、又化学成分の調整用に添加する珪石、ドロマ
イトなどの成分調整材も原料自体が砕石であるの
で混合して同時に融解すればよく、固体の均一混
合の問題はあつても炉の容積も大きく、従つて滞
留時間も長いために比較的問題は少なかつたが、
何よりも高炉から持ち出した莫大な熱量を放冷時
に放出して利用できず廃棄している結果となつて
いる。
Inorganic fibers called mineral wool, slag wool, rock wool, etc. are also manufactured by melting natural rocks and making them into cotton, but in Japan, they are most commonly made by adding composition adjustment materials to crushed blast furnace slag as necessary. It is added and remelted in a melting furnace such as an electric furnace or a cupola, and the molten material is fed to a cotton machine where centrifugal force and/or
Alternatively, a method of forming fibers using fluid pressure such as compressed air or steam has been adopted. This conventional method uses crushed slag stone, so it is convenient for transportation and storage of raw materials, and the raw materials themselves, such as silica stone and dolomite, which are added to adjust chemical components, are crushed stones, so they are mixed and melted at the same time. Even if there were problems with uniform mixing of solids, there were relatively few problems due to the large volume of the furnace and the long residence time.
Above all, the huge amount of heat taken out of the blast furnace is released when it is left to cool, resulting in it being unusable and being discarded.

そこで省エネルギーの観点より高炉からの高温
溶融スラグを電気炉に直接装入し、電気炉で成分
調整と温度調整を行つた後、製綿機に供給する方
法が注目されている。例えば特公昭37−4559号公
報に高滓綿製造法として記載されている。特公昭
59−131534号公報なども全く同じ技術内容のもの
である。これらの方法では、溶融スラグを電気炉
で僅かに加熱し、珪石等の成分調整材を溶融させ
るだけのエネルギー消費で済むので、従来方法に
比較して多大なエネルギーを節約することができ
る。しかし高炉のスラグ排出作業は数時間毎で間
欠的であり、鍋車で輸送された溶融スラグの電気
炉への装入も間欠的にならざるを得ない。一方、
ロツクウールの品質の安定化、歩留の向上のため
には製綿機への溶融物の成分と供給量をできるだ
け変動しないようにすることが肝要である。
Therefore, from the viewpoint of energy conservation, attention is being paid to a method in which high-temperature molten slag from a blast furnace is directly charged into an electric furnace, the composition and temperature are adjusted in the electric furnace, and then the slag is supplied to a cotton milling machine. For example, it is described in Japanese Patent Publication No. 37-4559 as a method for producing high slag cotton. Tokko Akira
Publication No. 59-131534 and the like have exactly the same technical content. In these methods, the energy consumption is only required to slightly heat the molten slag in an electric furnace and melt the composition adjusting material such as silica stone, so a large amount of energy can be saved compared to conventional methods. However, the slag discharge from the blast furnace is performed intermittently every few hours, and the molten slag transported by ladle truck must also be charged intermittently into the electric furnace. on the other hand,
In order to stabilize the quality of rock wool and improve the yield, it is important to minimize fluctuations in the composition and amount of melt fed to the cotton mill.

ロツクウール製綿に適当な成分となつている原
料溶融物中へ、輸送によつて冷却したスラグ溶融
物を添加すると成分と温度の不均一が起る。その
成分の調整のために、通常は浴面上へ計量かつ予
熱された珪石等の成分調整材を上方より投入して
いる。この成分調整材は予熱してあつても、浴の
温度よりはるかに低温度であるので、浴表面で互
いに固まつて均一に溶融しない問題点がある。
When a slag melt cooled during transport is added to a raw material melt which is a suitable constituent for rock wool cotton, non-uniformities in composition and temperature occur. In order to adjust the components, a preheated component adjusting material such as silica stone is usually poured onto the bath surface from above. Even if this component adjusting material is preheated, the temperature is much lower than the bath temperature, so there is a problem that it hardens together on the bath surface and does not melt uniformly.

この問題点の解決法ではないが、溶融炉の炉壁
カーボン煉瓦を保護する手段として、特開昭56−
113335号公報には電気炉の炉底から、又は電極を
通して中性または還元気泡ガスを吹込んで浴を均
質にすること、またこの気泡ガスと共に炭または
石油コークスのような粉塵還元添加物を浴中に吹
込むことで還元雰囲気を炉の囲い内に生じさせる
ことが記載されている。
Although it is not a solution to this problem, as a means to protect the furnace wall carbon bricks of a melting furnace,
Publication No. 113335 states that neutral or reducing bubble gas is blown into the bath from the bottom of the electric furnace or through the electrodes to make the bath homogeneous, and that a dust-reducing additive such as charcoal or petroleum coke is added to the bath together with the bubble gas. It is described that a reducing atmosphere is created within the furnace enclosure by blowing into the furnace enclosure.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところで、上記電気炉への成分調整材の添加
は、溶融炉内の原料溶融物中へ、輸送によつて冷
却したスラグ溶融物を注入した時に特に成分調整
のために必要である。しかし、この時には浴、特
に浴上部はスラグ溶融物の注入のために温度が下
つている。そこへ予熱したとはいえ400℃以下の
成分調整材を上方より装入すると、たとえ溶融し
易い粉粒状にして装入しても、浴中で互いに固ま
り、攪拌を行つてもなかなか均一に溶解しないと
いう問題点があつた。
Incidentally, the addition of the composition adjusting material to the electric furnace is particularly necessary for composition adjustment when the slag melt cooled during transportation is injected into the raw material melt in the melting furnace. However, at this time the temperature of the bath, especially the upper part of the bath, has dropped due to the injection of the slag melt. Even if it is preheated, if you charge the composition adjustment material below 400℃ from above, even if you charge it in powder form that is easy to melt, it will solidify together in the bath, and it will be difficult to dissolve it uniformly even if you stir it. The problem was that it didn't.

〔問題点を解決するための手段〕 本発明者等は前記のような問題点を解決するた
め種々研究を行つた結果、炉蓋を貫通して浴中へ
挿入したランス管を通じて不活性ガスを吹込んで
溶融浴を攪拌すると共に、この不活性ガス流と共
に成分調整材の粉を浴中へ添加すれば、成分調整
材を短時間に浴中に均一に溶解させる事ができる
事を見出し本発明を完成した。
[Means for Solving the Problems] The present inventors have conducted various studies to solve the above-mentioned problems, and as a result, they have devised a method for introducing inert gas through a lance pipe inserted into the bath through the furnace lid. The present inventors have discovered that by stirring the molten bath by blowing air into the bath, and adding powder of the component adjusting material into the bath along with this inert gas flow, the component adjusting material can be uniformly dissolved in the bath in a short time. completed.

すなわち本発明は、スラグ溶融物を加熱する電
気炉内に、炉内ガスをシールしながら挿入した上
下動可能なランス管を通じて、溶融物浴中へ不活
性ガス流と共に成分調整材を添加することを特徴
とするスラグ溶融物への成分調整材添加方法であ
る。又その方法を実施する装置としては、電気炉
炉蓋にてガスシール装置、仕切弁を通つて炉蓋を
貫通させ、かつ下端を炉内溶融物中に挿入した上
下動可能なランス管に不活性ガス導管を可撓性管
を介して接続すると共に、不活性ガス導管、可撓
性管、ランス管上部の何れかの個所において成分
調整材供給装置を接続させてなるスラグ溶融物へ
の成分調整材添加装置である。
That is, the present invention involves adding a component adjusting material into a melt bath along with an inert gas flow through a vertically movable lance tube inserted into an electric furnace for heating a slag melt while sealing the furnace gas. This is a method for adding a component adjusting agent to a slag melt, characterized by the following. The apparatus for carrying out this method includes a lance tube that penetrates the electric furnace lid through a gas sealing device and a gate valve, and whose lower end is inserted into the molten material in the furnace and is movable up and down. A method for adding components to a slag melt by connecting an active gas conduit through a flexible tube and connecting a component adjusting material supply device to any of the upper parts of the inert gas conduit, flexible tube, and lance tube. This is an adjustment material addition device.

本発明の方法を実施するには、電気炉内の溶融
物浴を炉蓋を貫通して浴中に挿入したランス管を
通じて、窒素ガス、アルゴンガス等の不活性ガス
を吹込んで攪拌する必要がある。溶融浴は1500℃
前後の高温であるので、炉の内張耐火物は黒鉛等
のカーボン質、又は炭化珪素質の耐火物が使用さ
れる。これは溶融浴が塩基性の強い高炉スラグを
主成分としているので、通常の酸化物系の耐火材
料は侵蝕を受け易く使用できない。カーボン質又
は炭化珪素質の耐火物であればスラグに対する濡
れ性も少なく、侵蝕も少ない。しかし、この種の
耐火物は酸素が存在すると高温で酸化消耗する弱
点がある。そこで炉内空間は窒素ガス等の不活性
ガスで充填し、正圧に保持して空気の侵入を防止
するようになつている。ガス吹込のランス管も、
同様の理由で少なくとも溶融物浴に浸る部分はカ
ーボン質、又は炭化珪素質の耐火材料を使用す
る。第2図で示すように、このランス管1は溶融
物液面で電極13をきつたと考えた時の3つの円
の外接円内に挿入することが好ましい。これは、
この部分が電流密度が最も大きい部分であり、従
つて温度が最も高く、かつ浴の粘度が最も低くな
るからである。特にランス管1をカーボン質、炭
化珪素質の導電性材料で構成し、第2図の符号1
の如く、電極13と電極13を結ぶ線上の中点に
挿入する時には、ランス管を媒介してその周辺の
電流密度が特に大きくなり、吹込位置の浴の粘度
は最も低くなる。このガス吹込により加熱された
低粘度溶融物は上昇し、浴面に達して炉壁へ向つ
て流れ、炉壁近くで下方流となつて対流攪拌と対
流伝熱が行われる。
To carry out the method of the present invention, it is necessary to stir the molten bath in the electric furnace by blowing inert gas such as nitrogen gas or argon gas through a lance tube inserted into the bath through the furnace lid. be. Melting bath is 1500℃
Since the temperature is high, carbonaceous materials such as graphite or silicon carbide refractories are used for the refractory lining of the furnace. Since the molten bath is mainly composed of highly basic blast furnace slag, ordinary oxide-based refractory materials cannot be used because they are susceptible to corrosion. Carbon or silicon carbide refractories have less wettability to slag and less corrosion. However, this type of refractory has the disadvantage of being oxidized and consumed at high temperatures in the presence of oxygen. Therefore, the space inside the furnace is filled with an inert gas such as nitrogen gas and maintained at a positive pressure to prevent air from entering. Gas injection lance pipe,
For the same reason, at least the portion immersed in the melt bath is made of carbon or silicon carbide refractory material. As shown in FIG. 2, this lance tube 1 is preferably inserted within the circumscribed circles of three circles when the electrode 13 is considered to be tight at the melt level. this is,
This is because this is the area where the current density is the highest, the temperature is the highest, and the viscosity of the bath is the lowest. In particular, the lance tube 1 is made of a conductive material such as carbon or silicon carbide, and the reference numeral 1 in FIG.
When the bath is inserted at the midpoint on the line connecting the electrodes 13 as shown in FIG. The low-viscosity melt heated by this gas injection rises, reaches the bath surface, flows toward the furnace wall, becomes a downward flow near the furnace wall, and convective stirring and convective heat transfer occur.

このランス管は、浸漬深さが浅すぎると吹込ガ
スが溶融物を動かす効果が少なく、反対に深すぎ
ると電極による加熱帯域を外れ粘度が最も低い所
へ吹込む事ができないばかりでなく、炉内ランス
管も長くなり、ランス管折損の危険も大きくな
る。そこでランス管は上下動可能に炉外の支持部
材により保持されている。このランス管は、炉内
の不活性ガスが漏洩しないようガスシール装置、
仕切弁を通つて炉蓋部を貫通している。このよう
に炉内ガスをシールしながら炉内へ挿入したラン
ス管を通つて浴攪拌用の不活性ガスを流し、この
ガス流中に珪石粉等の成分調整材粉を浮遊させて
ガスと共に浴中へ送り込む。珪石粉の粒径として
は、ガス中に浮遊させるため5mm以下、好ましく
は2mm以下が好ましい。ガス流速は5m/sec以
上、好ましくは10m/sec以上とする。
If this lance tube is immersed too shallowly, the blowing gas will have little effect on moving the molten material.On the other hand, if it is too deep, it will not only be out of the heating zone by the electrode and unable to blow into the lowest viscosity area, but also The inner lance tube also becomes longer, increasing the risk of the lance tube breaking. Therefore, the lance tube is held by a support member outside the furnace so as to be able to move up and down. This lance tube is equipped with a gas seal device to prevent inert gas from leaking inside the furnace.
It passes through the furnace lid through the gate valve. In this way, while sealing the gas in the furnace, inert gas for bath stirring is flowed through the lance tube inserted into the furnace, and powdered composition adjusting materials such as silica powder are suspended in this gas flow, and the mixture is bathed together with the gas. Send it inside. The particle size of the silica powder is preferably 5 mm or less, preferably 2 mm or less so that it can be suspended in the gas. The gas flow rate is 5 m/sec or more, preferably 10 m/sec or more.

攪拌ガスの流速により調整材の粒度を調整す
る。即ち流速が小であれば粒度も細かくする。炉
内ガスは勿論、一定の正圧を保ちつつ、この攪拌
用ガス吹込量だけ排出口を通じて外部へ排出す
る。成分調整材は予め燃焼ガス等により予熱され
ており、秤量されたのち、ホツパーに貯留され、
ホツパー下部の定量供給装置により不活性ガス中
に送り込まれる。また、他の方法としてホツパー
の下部より循環ガスを吹込んでホツパー内を調整
材の流動層とし、この流動層の一部を不活性ガス
のエゼクター効果により調整材を吸引して、ガス
中に流動させるようにしてもよい。
The particle size of the conditioning material is adjusted by the flow rate of the stirring gas. That is, if the flow rate is low, the particle size is also fine. The gas in the furnace is, of course, discharged to the outside through the discharge port while maintaining a constant positive pressure. The component adjustment material is preheated by combustion gas, etc., and after being weighed, it is stored in a hopper.
It is fed into the inert gas by a metering device at the bottom of the hopper. Another method is to blow circulating gas from the bottom of the hopper to create a fluidized bed of the conditioning material inside the hopper, and use a portion of this fluidized bed to suck the conditioning material through the ejector effect of an inert gas, causing it to flow into the gas. You may also do so.

本発明方法を実施する装置としては、ランス管
を上下動させるため、ランス管の上端部には可撓
性管を接続し、該可撓性管を不活性ガス導管に接
続する。ランス管の炉蓋貫通部には、ランス管取
替のための引抜および挿入時に炉内ガスをシール
し、また常時でも炉内ガスをシールする目的で、
グランドパツキン又はメカニカルシール等のガス
シール装置とスライド式ゲート弁等の仕切弁を、
例えば(シール装置)−(仕切弁)−(シール装置)
という組合せで取付ける。
In an apparatus for carrying out the method of the present invention, in order to move the lance tube up and down, a flexible tube is connected to the upper end of the lance tube, and the flexible tube is connected to an inert gas conduit. The lance tube's passage through the furnace cover is designed to seal the furnace gas when it is pulled out and inserted to replace the lance tube, and also to seal the furnace gas at all times.
Gas seal devices such as gland seals or mechanical seals and gate valves such as slide gate valves,
For example, (seal device) - (gate valve) - (seal device)
Install with this combination.

上下動機構としては、ランス管の上部を、支持
部材に摺動又はガイド車による転動可能に保持さ
せ、このガイド車をワイヤ又はチエーンとこれを
駆動する駆動モータで上下動させるか、このガイ
ド車をラツク・ピニオン機構により上下動させる
ようにしてもよい。
As for the vertical movement mechanism, the upper part of the lance tube is held so that it can slide on a support member or can be rolled by a guide wheel, and the guide wheel is moved up and down by a wire or chain and a drive motor that drives it, or The vehicle may be moved up and down by a rack and pinion mechanism.

成分調整材供給装置からの導管を接続させる位
置としては、不活性ガス導管、可撓性管又はラン
ス管上部の何れの個所でもよい。管が固定されて
いるという点からは不活性ガス導管が好都合であ
るが、不活性ガス導管又は可撓性管に接続させる
と、通常、不活性ガス流により調整材粉を流動化
して上方へ持ち上げる部分を生ずる。この場合に
は前記の攪拌ガス量と導管の内径によりガス流速
が定まり、これにより流動化して持ち上げる最大
粒径が定まつてくる。これに対し、ランス管上部
に接続すると、上下動するので接続導管を伸縮管
により接続しなければならない欠点はあるが、ガ
ス流速にくらべ、調整材の粒径が大きくても、重
力による落し込みにより炉内に送り込み得る。即
ちガス量による調整材粒径の制約がなくなるとい
う利点がある。この場合には、成分調整材貯留ホ
ツパーをランス管より充分高く位置させると共
に、ホツパーからランス管までの間に上昇部をな
くし、一方的に下降するよう内外2重管よりなる
伸縮管を使用するなどの装置が好ましい。
The conduit from the component adjusting material supply device may be connected to any of the inert gas conduit, the flexible tube, or the upper part of the lance tube. Although an inert gas conduit is advantageous in that the tube is fixed, when connected to an inert gas conduit or flexible tube, the inert gas flow typically fluidizes the conditioning powder and moves it upward. Creates a part to lift. In this case, the gas flow rate is determined by the above-mentioned stirring gas amount and the inner diameter of the conduit, which determines the maximum particle size that can be fluidized and lifted. On the other hand, when connected to the upper part of the lance pipe, it moves up and down, so the connecting conduit must be connected with an expandable pipe, but even if the particle size of the adjusting material is large compared to the gas flow rate, it will not fall due to gravity. can be fed into the furnace by That is, there is an advantage that there is no restriction on the particle size of the adjusting material depending on the amount of gas. In this case, the component adjustment material storage hopper should be located sufficiently higher than the lance pipe, and there should be no rising part between the hopper and the lance pipe, and a telescopic pipe consisting of an inner and outer double pipe should be used so that it descends unilaterally. A device such as is preferred.

〔実施例〕〔Example〕

次に本発明に係る装置の実施例を図面について
説明する。第1図はランス管の上下動手段を支持
部材に対してガイド車の転動方式とし、その駆動
をワイヤと減速機付モーターとで行ない、調整材
の添加を不活性ガス導管により送入する場合であ
る。1は炭素質ランス管であり、これは必要によ
り炉内に入る部分のみ黒鉛管とし、上部を金属管
としてもよい。2はゴム又は合成樹脂または金属
製の可撓性管で、炭素質ランス管1の上下動に対
応する。3は不活性ガス導管、4は炭素質ランス
管1のガイド車、5はその転動輪である。6は炭
素質ランス管1の支持部材であり、ガイド車4は
この支持部材6に転動輪5を介して支持されてい
る。ガイド車4はワイヤ7と減速機付モーター8
により駆動される。12は電気炉であり、炭素質
ランス管1は、この炉蓋部でガスシール装置9、
10及び仕切弁11により炉内ガスをシールして
いる。成分調整材15は秤量及び予熱された後、
成分調整材貯留ホツパー14内に貯留される。こ
の量は電気炉12に装入される溶融スラグ量に対
応して定められる。成分調整材15は定量供給装
置6により少量ずつ不活性ガス流に添加され、流
動化されて不活性ガスと共に炉内溶融中に装入さ
れる。
Next, an embodiment of the apparatus according to the present invention will be described with reference to the drawings. Figure 1 shows that the means for moving the lance tube up and down is a rolling system of a guide wheel relative to the support member, and the drive is performed by a wire and a motor with a speed reducer, and the adjustment material is added through an inert gas conduit. This is the case. 1 is a carbonaceous lance tube, and if necessary, only the portion that enters the furnace may be a graphite tube, and the upper portion may be a metal tube. 2 is a flexible tube made of rubber, synthetic resin, or metal, and corresponds to the vertical movement of the carbonaceous lance tube 1. 3 is an inert gas conduit, 4 is a guide wheel for the carbonaceous lance tube 1, and 5 is a rolling wheel thereof. 6 is a support member for the carbonaceous lance tube 1, and the guide wheel 4 is supported by this support member 6 via a rolling wheel 5. The guide wheel 4 includes a wire 7 and a motor 8 with a reduction gear.
Driven by. 12 is an electric furnace, and the carbonaceous lance tube 1 has a gas sealing device 9,
10 and a gate valve 11 to seal the gas inside the furnace. After the component adjustment material 15 is weighed and preheated,
It is stored in the component adjustment material storage hopper 14. This amount is determined in accordance with the amount of molten slag charged into the electric furnace 12. The component adjusting material 15 is added little by little to the inert gas stream by the quantitative feeder 6, fluidized, and charged into the furnace together with the inert gas during melting.

第3図は支持部材にラツクギアを兼ねさせ、ガ
イド車に減速機付モーターとこれに駆動されるピ
ニオンギアを載置し、ラツク・ピニオン機構によ
りランス管を駆動すると共に成分調整材をランス
管の上部、ガイド車の部分で不活性ガスに合流さ
せ、伸縮管により重力を利用して調整材を炉内に
ガスと共に送入した例である。18はラツクギア
であり、支持部材を兼ねている。19は炭素質ラ
ンス管1を上下動させるピニオンギアである。1
7は内外2重管よりなる伸縮管であり、上部では
ガスが漏洩しないようにシールしている。この実
施例の場合には、ラツクギア18と成分調整材貯
留ホツパー14を電気炉12と一体に取付け、成
分調整材貯留ホツパー14の上端をスイベル・ジ
ヨイント、その他の可撓性管で予熱器に接続する
ことにより電気炉12の傾動にラツクギア18や
成分調整材貯留ホツパが追従できるようにしてあ
る。
In Fig. 3, the support member also serves as a rack gear, a motor with a reduction gear and a pinion gear driven by this are mounted on the guide wheel, and the lance tube is driven by the rack and pinion mechanism, and the composition adjustment material is applied to the lance tube. This is an example in which the adjustment material is merged with inert gas at the upper part of the guide wheel, and sent into the furnace together with the gas using gravity through a telescoping tube. 18 is a rack gear, which also serves as a support member. 19 is a pinion gear that moves the carbonaceous lance tube 1 up and down. 1
Reference numeral 7 denotes an extensible tube consisting of an inner and outer double tube, and the upper part is sealed to prevent gas from leaking. In the case of this embodiment, the rack gear 18 and the component adjustment material storage hopper 14 are installed integrally with the electric furnace 12, and the upper end of the component adjustment material storage hopper 14 is connected to the preheater with a swivel joint or other flexible tube. This allows the rack gear 18 and the component adjustment material storage hopper to follow the tilting movement of the electric furnace 12.

次に上記装置を利用した場合の実施例について
説明する。
Next, an example in which the above device is used will be described.

電気炉中のロツクウール原料溶融物に、高炉溶
融スラグ5tを装入し、炉蓋部より挿入した黒鉛ラ
ンス管を通じて窒素ガスを吹込み、溶融浴を攪拌
しながら2mm以下の粒径に粉砕し、秤量したのち
350℃に予熱した珪石粉500Kgを25Kg/minで窒素
ガス流に浮遊させながら添加し、炉内に送入し
た。その結果、珪石粉を浴面へ一度に添加した従
来方法の場合は、完全溶解に40分以上を要し、不
溶解の塊が電極折損や炉壁損耗の原因となつてい
たのが、上記実施例では装入と同時に殆んど完全
に溶解しているのが認められた。
5 tons of blast furnace molten slag is charged into the rock wool raw material melt in an electric furnace, nitrogen gas is blown through a graphite lance tube inserted from the furnace lid, and the molten bath is pulverized to a particle size of 2 mm or less while stirring. After weighing
500 kg of silica powder preheated to 350°C was added at a rate of 25 kg/min while floating in a nitrogen gas flow and fed into the furnace. As a result, in the case of the conventional method in which silica powder was added to the bath surface all at once, it took more than 40 minutes for complete dissolution, and undissolved lumps caused electrode breakage and furnace wall damage. In the examples, almost complete dissolution was observed upon charging.

〔効果〕〔effect〕

電気炉中のロツクウール原料溶融物は連続的に
製綿機に排出され、炉内原料が一定量以下となる
と高炉溶融スラグが装入される。この時、輸送に
よりスラグ温度が低下しているので、浴温度が低
下する。ここへ予熱されてはいるが400℃以下の
成分調整材を一度に浴表面に添加すると互いに固
まつて塊をなし、完全溶解に長時間を要し、この
塊が電極折損や炉壁損耗の原因となつていたの
が、本発明によれば成分調整材を攪拌ガスと共に
少量ずつ添加することにより、添加と同時に完全
に溶解し、塊を形成することがないので、浴の成
分を短時間に均一に調整できるばかりでなく、電
極折損や炉壁損耗の原因を排除することができ
た。
The rock wool raw material melt in the electric furnace is continuously discharged to the cotton mill, and when the raw material in the furnace reaches a certain amount or less, blast furnace molten slag is charged. At this time, since the slag temperature is lowered due to transportation, the bath temperature is lowered. If preheated but below 400℃ component adjustment materials are added to the bath surface all at once, they will solidify together and form lumps, which will take a long time to completely dissolve, and these lumps will cause electrode breakage and furnace wall damage. However, according to the present invention, by adding the component adjustment material little by little together with the stirring gas, the component is completely dissolved at the same time as the addition, and no lumps are formed. Not only was it possible to uniformly adjust the temperature, but the causes of electrode breakage and furnace wall damage were also eliminated.

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

第1図は本発明のスラグ溶融物への成分調整材
添加装置の一実施例を示す垂直断面図、第2図は
電極間のランス管挿入最適個所を示した水平断面
図、第3図は本発明のスラグ溶融物への成分調整
材添加装置の他の実施例を示す垂直断面図であ
る。 1……炭素質ランス管、2……可撓性管、3…
…不活性ガス導管、9……ガスシール装置、10
……ガスシール装置、11……仕切弁、12……
電気炉、14……成分調整材貯留ホツパー、15
……成分調整材、16……定量供給装置。
Fig. 1 is a vertical sectional view showing an embodiment of the device for adding composition adjusting material to molten slag according to the present invention, Fig. 2 is a horizontal sectional view showing the optimal lance tube insertion point between the electrodes, and Fig. 3 is FIG. 3 is a vertical cross-sectional view showing another embodiment of the device for adding a component adjusting material to a slag melt according to the present invention. 1... Carbonaceous lance tube, 2... Flexible tube, 3...
...Inert gas conduit, 9...Gas seal device, 10
...Gas seal device, 11...Gate valve, 12...
Electric furnace, 14...Component adjustment material storage hopper, 15
...Component adjustment material, 16...Quantitative supply device.

Claims (1)

【特許請求の範囲】 1 スラグ溶融物を加熱する電気炉内に炉内ガス
をシールしながら挿入した上下動可能なランス管
を通じて、溶融物浴中へ不活性ガス流と共に成分
調整材を添加することを特徴とするスラグ溶融物
への成分調整材添加方法。 2 電気炉炉蓋にてガスシール装置、仕切弁を通
つて炉蓋を貫通させ、かつ下端を炉内溶融物中に
挿入した上下動可能なランス管に不活性ガス導管
を可撓性管を介して接続すると共に、不活性ガス
導管、可撓性管、ランス管上部の何れかの個所に
おいて成分調整材供給装置を接続させてなるスラ
グ溶融物への成分調整材添加装置。 3 成分調整材供給装置が成分調整材貯留ホツパ
ーの下端部に定量供給装置を設けたものである特
許請求範囲第2項記載のスラグ溶融物への成分調
整材添加装置。
[Claims] 1. A component adjusting material is added into the melt bath along with an inert gas flow through a vertically movable lance tube inserted into an electric furnace for heating the slag melt while sealing the furnace gas. A method for adding a composition adjusting agent to a slag melt, characterized by: 2 At the electric furnace lid, an inert gas conduit is passed through the furnace lid through a gas sealing device and a gate valve, and an inert gas conduit is inserted into a vertically movable lance tube whose lower end is inserted into the melt in the furnace. A device for adding a component adjusting material to a molten slag, which is connected to the inert gas conduit, the flexible tube, or the upper part of the lance tube. 3. An apparatus for adding a composition adjusting material to a molten slag according to claim 2, wherein the composition adjusting material supplying apparatus is provided with a quantitative feeding apparatus at the lower end of a composition adjusting material storage hopper.
JP23448486A 1986-10-03 1986-10-03 Addition of component controlling material to slag melt and equipment therefor Granted JPS6389439A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23448486A JPS6389439A (en) 1986-10-03 1986-10-03 Addition of component controlling material to slag melt and equipment therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23448486A JPS6389439A (en) 1986-10-03 1986-10-03 Addition of component controlling material to slag melt and equipment therefor

Publications (2)

Publication Number Publication Date
JPS6389439A JPS6389439A (en) 1988-04-20
JPH0469575B2 true JPH0469575B2 (en) 1992-11-06

Family

ID=16971744

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23448486A Granted JPS6389439A (en) 1986-10-03 1986-10-03 Addition of component controlling material to slag melt and equipment therefor

Country Status (1)

Country Link
JP (1) JPS6389439A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03115138A (en) * 1989-09-28 1991-05-16 Toshio Shiina Method for adding component modifier to molten slag

Also Published As

Publication number Publication date
JPS6389439A (en) 1988-04-20

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