JPH0754281Y2 - Smelting reduction furnace - Google Patents

Smelting reduction furnace

Info

Publication number
JPH0754281Y2
JPH0754281Y2 JP7031290U JP7031290U JPH0754281Y2 JP H0754281 Y2 JPH0754281 Y2 JP H0754281Y2 JP 7031290 U JP7031290 U JP 7031290U JP 7031290 U JP7031290 U JP 7031290U JP H0754281 Y2 JPH0754281 Y2 JP H0754281Y2
Authority
JP
Japan
Prior art keywords
furnace
molten metal
smelting reduction
injection
flue
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 - Fee Related
Application number
JP7031290U
Other languages
Japanese (ja)
Other versions
JPH0429646U (en
Inventor
充晴 岸本
慶吉 村上
義雄 内山
健一 矢島
賢 滝浦
聡 辰田
幸彦 高座
寿美男 佐藤
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.)
Kawasaki Motors Ltd
Original Assignee
Kawasaki Jukogyo KK
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 Kawasaki Jukogyo KK filed Critical Kawasaki Jukogyo KK
Priority to JP7031290U priority Critical patent/JPH0754281Y2/en
Publication of JPH0429646U publication Critical patent/JPH0429646U/ja
Application granted granted Critical
Publication of JPH0754281Y2 publication Critical patent/JPH0754281Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【考案の詳細な説明】 [産業上の利用分野] この考案は、鉄鉱石などを溶融状態で還元するための金
属浴炉式の溶融還元炉に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention relates to a metal bath furnace type smelting reduction furnace for reducing iron ore or the like in a molten state.

[従来の技術] 溶融還元法は、鉄鉱石(酸化鉄)などの金属酸化物を含
有する鉱石を、溶融状態で還元して鉄やフェロアロイを
得る方法であり、高炉法などに代わる金属製造法として
近年、注目を集める技術である。
[Prior Art] The smelting reduction method is a method of obtaining an iron or ferroalloy by reducing an ore containing a metal oxide such as iron ore (iron oxide) in a molten state, and is an alternative to the blast furnace method. It is a technology that has attracted attention in recent years.

溶融還元法には種々のプロセスが提案されており、還元
炉の形式も多様であるが、代表的な形式としていわゆる
金属浴炉式の溶融還元炉があげられる。これは、例えば
製鉄用のものでは、溶湯(スラグ浴を含む鉄浴)内に石
炭、石灰および酸素とともに鉄鉱石(または予備還元鉄
などの鉱石)を装入し、これを還元して溶融銑鉄を得る
還元炉であるが、反応が速く、設備形式がシンプルであ
るなどの理由で多くのプロセスに採用されている。
Various processes have been proposed for the smelting reduction method, and there are various types of reducing furnaces, but a typical type is a so-called metal bath furnace type smelting reduction furnace. For ironmaking, for example, molten iron (or iron bath including slag bath) is charged with iron ore (or ore such as pre-reduced iron) together with coal, lime and oxygen, and this is reduced to produce molten pig iron. Although it is a reducing furnace, it is used in many processes because of its fast reaction and simple equipment type.

金属浴炉式の溶融還元炉は、溶融金属を保持する点で溶
鋼の精錬炉である転炉と共通することなどから、従来
は、第6図のように傾動可能な転炉型炉51が一般的であ
った。なお、同種の溶融還元炉は、例えば実公平1−36
903号公報に記載されている。また、溶融還元炉に転炉
型炉が用いられている他の理由は、溶融還元法では、作
業が本来バッチ式で、第6図に示すように作業を開始す
る際に炉51内に種湯(溶融金属)を注入する必要があ
り、この種湯をレードル52などを用いて注入するのに、
炉51を傾動できる方が注入作業が楽であること、また還
元された溶融金属を炉51内から取り出すのに、炉51を傾
動すれば簡単に行えることである。
Since a metal bath furnace type smelting reduction furnace is common with a converter which is a refining furnace for molten steel in that it holds molten metal, conventionally, a tiltable converter furnace 51 as shown in FIG. 6 has been used. It was common. In addition, the same type of smelting reduction furnace is, for example,
No. 903. Another reason why the converter furnace is used as the smelting reduction furnace is that in the smelting reduction method, the work is originally a batch type, and as shown in FIG. It is necessary to inject hot water (molten metal), and to inject this hot water using a ladle 52 etc.,
The fact that the furnace 51 can be tilted makes the injection work easier, and it is easy to take out the reduced molten metal from the furnace 51 by tilting the furnace 51.

そして、炉体上方にはやはり転炉の場合と同様、軸心位
置に開口(炉口)部を有し、これに昇降式のヘッド53を
介して煙道(ダクト)54が接続されて炉51内の発生ガス
を排出するようになっている。これは、還元時に炉内で
は高温で還元力を有するCO(一酸化炭素)ガスが多量に
発生するので、このガスを処理設備へ送ったり、あるい
は、溶融還元炉に投入する前の鉄鉱石を装入した予備還
元炉に導き、鉄鉱石の予備還元に利用したりするためで
ある。また前記ガスは可燃成分を含むので、空気中の酸
素と接触すると急激に燃焼するため、煙道や炉体には窒
素ガスなどの不活性ガスを噴射する設備が設けられてい
る。
As in the case of the converter, there is an opening (furnace opening) at the axial center position above the furnace body, and a flue (duct) 54 is connected to this through an elevating head 53 and the furnace is connected. The gas generated inside 51 is discharged. This is because a large amount of CO (carbon monoxide) gas, which has reducing power at high temperature, is generated in the furnace at the time of reduction, so this gas is sent to treatment equipment or iron ore before being put into the smelting reduction furnace. This is because it is used for pre-reduction of iron ore by leading it to the charged pre-reduction furnace. Further, since the gas contains combustible components, it rapidly burns when it comes into contact with oxygen in the air. Therefore, equipment for injecting an inert gas such as nitrogen gas is provided in the flue and the furnace body.

[考案が解決しようとする課題] しかしながら、上記した転炉型溶融還元炉については下
記のような問題点があった。すなわち、(a)炉を傾動
する際、炉口と煙道を接続するヘッドを上昇させられる
ように、ヘッドを遠隔操作で昇降可能な構造(例えば、
特開平1−252891号)にする必要がある。このため、ヘ
ッドの構造が複雑になり、設備費が膨大なうえに、故障
しやすく、メンテナンスに手間がかかる。
[Problems to be Solved by the Invention] However, the above-mentioned converter-type smelting reduction furnace has the following problems. That is, (a) when tilting the furnace, the head that connects the furnace mouth and the flue can be raised by a remote operation so that the head can be raised (for example,
It is necessary to use Japanese Patent Laid-Open No. 1-252891). For this reason, the structure of the head becomes complicated, the equipment cost is enormous, the head is easily broken, and the maintenance is troublesome.

(b)溶融金属の注入時に、炉と煙道とは完全に切り離
されるので、炉内のガスが外部に逃げ、また煙道内に空
気が混入する。したがって、ガスの回収率が低下し、予
備還元などに有効に利用できなくなり、また炉内に溶融
金属を注入した後で、煙道および炉内に混入した空気を
不活性ガスでパージさせる必要がある。このパージには
多量の不活性ガスを要するので、コストがかかるうえ
に、時間(通常は、20〜30分)もかかり、稼働率が低下
する。
(B) When the molten metal is injected, the furnace and the flue are completely separated from each other, so that the gas in the furnace escapes to the outside and air is mixed in the flue. Therefore, the recovery rate of the gas decreases, it cannot be effectively used for preliminary reduction, etc., and it is necessary to purge the air mixed in the flue and the furnace with an inert gas after injecting the molten metal into the furnace. is there. Since a large amount of inert gas is required for this purging, it is costly and also takes time (usually 20 to 30 minutes), resulting in a low operating rate.

この考案は上述の問題点を解決するためになされたもの
で、炉を傾動させずに、溶融金属の注入および還元溶融
金属の出湯を可能にすることにより、炉と煙道とを常時
接続しておくことができ、ヘッドを省いたり又はその構
造を簡素化したりして設備費の大幅な低減が図れ、また
溶融金属の注入後に不活性ガスで空気をパージする必要
がなく、稼働率を向上し得る溶融還元炉を提供すること
を目的としている。
The present invention has been made to solve the above-mentioned problems, and enables the molten metal to be injected and the reduced molten metal to be discharged without tilting the furnace so that the furnace and the flue are always connected. The cost can be reduced by omitting the head or simplifying the structure, and the facility cost can be significantly reduced. Also, it is not necessary to purge the air with an inert gas after injecting the molten metal, improving the operation rate. The purpose is to provide a smelting reduction furnace that can be used.

[課題を解決するための手段] 上記した目的を達成するために本考案の溶融還元炉は、
a)炉の炉口に煙道を直接又はヘッドを介して接続し、
b)該炉の底部に開閉可能な出湯孔を設け、c)前記炉
の上部又は煙道に溶融金属の注入孔を開設し、d)該注
入孔に溶融金属の注入部を接続すると共に、e)注入孔
と注入部との間に又は注入部の受入れ口に閉塞機構を設
けている。
[Means for Solving the Problems] In order to achieve the above object, the smelting reduction furnace of the present invention is
a) connecting the flue to the furnace mouth directly or via the head,
b) a tap hole that can be opened and closed is provided at the bottom of the furnace, c) a molten metal injection hole is opened at the top of the furnace or a flue, and d) a molten metal injection part is connected to the injection hole, e) A blocking mechanism is provided between the injection hole and the injection section or at the receiving port of the injection section.

また請求項2記載のように、f)前記注入孔と前記注入
部との間に、それぞれ閉塞機構を介在して溶融金属の貯
留タンクを介設し、g)該貯留タンクに高圧の不活性ガ
スの導入管を接続することが好ましい。
Further, as described in claim 2, f) a molten metal storage tank is provided between the injection hole and the injection portion with a closing mechanism interposed therebetween, and g) a high-pressure inert gas in the storage tank. It is preferable to connect a gas introduction pipe.

[作用] 上記の構成を有する本考案の溶融還元炉によれば、例え
ば注入部の受け入れ口側にだけ閉塞機構を備えた炉で
は、炉内に窒素ガスなどの不活性ガスを吹き込んで、炉
内を大気圧よりもやや高くする。それから、閉塞機構を
開放して注入部内に溶融金属を注入し、閉塞機構を閉じ
て注入部を密閉した状態で、炉の圧力をやや下げて炉内
に溶融金属を注入する。こうして、種湯としての溶融金
属が炉内に注入された状態で、原料としての鉱石を石炭
などの副原料とともに炉内に装入し、酸素を吹き込んで
溶融状態で還元させる。還元作業が終了すると、炉底部
の出湯孔をホールオープナーなどで開口し、出湯する。
この結果、炉と煙道を接続するヘッドの、炉口への着脱
や昇降動作が不要になり、また煙道や炉内に流入した空
気を不活性ガスでパージさせる作業も必要でなくなる。
[Operation] According to the smelting reduction furnace of the present invention having the above-mentioned configuration, for example, in a furnace having a closing mechanism only on the inlet side of the injection part, an inert gas such as nitrogen gas is blown into the furnace to Make the inside a little higher than atmospheric pressure. Then, the closing mechanism is opened to inject the molten metal into the pouring portion, and the closing mechanism is closed to close the pouring portion to slightly lower the pressure of the furnace and inject the molten metal into the furnace. Thus, in the state where the molten metal as the seed water is injected into the furnace, the ore as the raw material is charged into the furnace together with the auxiliary raw material such as coal, and oxygen is blown to reduce the molten ore in the molten state. When the reduction work is completed, the tap hole at the bottom of the furnace is opened with a hole opener or the like, and tap water is tapped.
As a result, it is not necessary to attach or detach the head for connecting the furnace and the flue to the furnace mouth or to move up and down, and it is not necessary to purge the air flowing into the flue or the furnace with an inert gas.

請求項2記載の溶融還元炉によれば、貯留タンクと注入
孔との間の閉塞機構を閉じた状態で、注入部との間の閉
塞機構を開放し、タンク内に不活性ガスを吹き込んで空
気をパージさせた後、タンク内に注入部から溶融金属を
注入する。そして注入部側の閉塞機構を閉じ、注入孔側
の閉塞機構を開放して、タンク内の溶融金属を炉内に注
入する。これにより、炉と外界とを完全に遮断した状態
で、溶融金属が炉内へ注入される。
According to the smelting reduction furnace of claim 2, in a state where the closing mechanism between the storage tank and the injection hole is closed, the closing mechanism between the injection part and the injection portion is opened, and the inert gas is blown into the tank. After purging the air, the molten metal is injected into the tank from the injection part. Then, the closing mechanism on the injection part side is closed, the closing mechanism on the injection hole side is opened, and the molten metal in the tank is injected into the furnace. As a result, the molten metal is injected into the furnace with the furnace completely isolated from the outside.

[実施例] 以下、本考案の溶融還元炉の実施例を図面に基づいて説
明する。
[Embodiment] An embodiment of the smelting reduction furnace of the present invention will be described below with reference to the drawings.

第1図は本考案の溶融還元炉を備えた製鉄用の溶融還元
系統図である。同図において、溶融還元炉1および予備
還元炉25は共に傾動型ではなく固定型炉からなり、予備
還元炉25で鉄鉱石を固体状態で予備還元した後、溶融還
元炉1で溶融状態で最終還元を行う一方、溶融還元炉1
において発生する高温で還元力のあるガスの一部を予備
還元炉25へ導入する主系統のほか、予備還元炉25を出た
ガスを、集塵器30を通してダスト分を除いた後、ガスホ
ルダー31に貯留する系統を有している。
FIG. 1 is a smelting reduction system diagram for iron making equipped with the smelting reduction furnace of the present invention. In the figure, both the smelting reduction furnace 1 and the preliminary reduction furnace 25 are fixed type furnaces, not tilting type furnaces. After preliminary reduction of iron ore in a solid state in the preliminary reduction furnace 25, final reduction in a molten state is performed in the smelting reduction furnace 1. While performing reduction, smelting reduction furnace 1
In addition to the main system that introduces a part of the high-temperature reducing gas generated in the preliminary reduction furnace 25, the gas that has flowed out of the preliminary reduction furnace 25 is removed through the dust collector 30 to remove dust, and then the gas holder It has a storage system at 31.

溶融還元炉1は転炉形状であるが、上記したとおり傾動
装置をもたない固定型炉で、内面に耐火材が装着されて
いる。炉1の底部付近には出湯孔2が穿設され、通常
(出湯時以外)は旧来の高炉出銑口と同様に閉塞材(マ
ッド)で閉塞されるが、ホールオープナーなどで開口す
ることにより必要に応じて開口し出湯できるようになっ
ている。
Although the smelting reduction furnace 1 has a converter shape, it is a fixed type furnace having no tilting device as described above, and a refractory material is attached to the inner surface thereof. A tap hole 2 is formed near the bottom of the furnace 1, and normally (except when tapping) is closed with a plug (mud) like the conventional blast furnace tap, but by opening with a hole opener, etc. It can be opened and tapped when necessary.

溶融還元炉1の上端の炉口3には、煙道4が直結され、
ランス5が煙道4を貫通して溶融還元炉1の軸心位置に
挿入されている。炉1の底部に、銑鉄浴Bの攪拌用窒素
ガスの吹き込みノズル6が設けられ、また炉1の上端部
にパージ用の窒素ガス導入管7が接続されている。
The flue 4 is directly connected to the furnace opening 3 at the upper end of the smelting reduction furnace 1,
A lance 5 penetrates the flue 4 and is inserted in the axial center position of the smelting reduction furnace 1. A nitrogen gas blowing nozzle 6 for stirring the pig iron bath B is provided at the bottom of the furnace 1, and a nitrogen gas introducing pipe 7 for purging is connected to the upper end of the furnace 1.

前記溶融還元炉1の上部には、溶鉄(種湯)Aの注入孔
8が穿設されている。また、前記予備還元炉25で予備還
元した鉄鉱石の装入路9および石炭、石灰などの装入路
10が、それぞれ炉1の上部に接続されている。
An injection hole 8 for molten iron (seed bath) A is formed in the upper portion of the smelting reduction furnace 1. Further, a charging path 9 for the iron ore preliminarily reduced in the preliminary reduction furnace 25 and a charging path for coal, lime, etc.
10 are each connected to the top of the furnace 1.

11は溶鉄Aの注入部で、この注入部11は本実施例では、
上端開口に閉塞機構としての密閉蓋12を備えた漏斗状注
入容器からなる。そして注入容器11の下端出口は、注入
管13を介して前記注入孔8に接続されている。注入容器
11の上端部に、高圧窒素ガスの導入管14、および開閉バ
ルブ15aを備えた排気管15がそれぞれ接続されている。
11 is an injection part of molten iron A, and this injection part 11 is
The funnel-shaped injection container is provided with a closed lid 12 as a closing mechanism at the upper end opening. The lower end outlet of the injection container 11 is connected to the injection hole 8 via an injection pipe 13. Infusion container
A high-pressure nitrogen gas introduction pipe 14 and an exhaust pipe 15 equipped with an opening / closing valve 15a are connected to the upper end of 11.

上記した構成からなる本実施例の溶融還元炉では、次の
ようにして溶融還元製鉄法が実施される。
In the smelting reduction furnace of this embodiment having the above-mentioned configuration, the smelting reduction iron-making method is carried out as follows.

まず、スタートアップ時、炉1内に窒素ガスを吹き込ん
で、炉1内を大気圧よりもやや高くする。それから、密
閉蓋12を開放して注入容器11に溶鉄Aを注入した後、密
閉蓋12を閉じて注入容器11内を密閉する。この状態で、
炉1の圧力をやや下げて注入容器11内の溶鉄Aを炉1内
に注入する。こうして、炉1と外界とを遮断した状態に
おいて、種湯としての溶鉄Aを炉1内に注入した後、鉄
鉱石および石炭、石灰などを炉1内に装入し、ランス5
から酸素を吹き込んで操業を開始する。すなわち、ラン
ス5から酸素が吹き込まれ、鉄鉱石は溶融状態で還元さ
れて銑鉄となる。還元反応に伴ってCOを多量に含んだ還
元力のある高温ガスが発生するが、このガスは煙道4を
通り、その大部分がサイクロン24でダストが取り除か
れ、予備還元炉25へ導入され、鉄鉱石の予備還元に使用
される。また残りのガスは、集塵器30でダストが取り除
かれた後、ガスホルダー31に貯留され、燃料として利用
される。
First, at the time of startup, nitrogen gas is blown into the furnace 1 so that the inside of the furnace 1 is slightly higher than atmospheric pressure. Then, the sealing lid 12 is opened to inject the molten iron A into the injection container 11, and then the sealing lid 12 is closed to seal the inside of the injection container 11. In this state,
The pressure of the furnace 1 is slightly lowered and the molten iron A in the injection container 11 is injected into the furnace 1. In this way, in a state where the furnace 1 and the outside world are cut off, molten iron A as seed water is injected into the furnace 1, and then iron ore, coal, lime, etc. are charged into the furnace 1, and the lance 5
Blows in oxygen to start operation. That is, oxygen is blown from the lance 5, and the iron ore is reduced in a molten state to become pig iron. A high-temperature gas containing a large amount of CO and having a reducing power is generated along with the reduction reaction, but this gas passes through the flue 4 and most of it is dusted by the cyclone 24 and introduced into the preliminary reduction furnace 25. , Used for preliminary reduction of iron ore. The remaining gas is stored in the gas holder 31 and used as fuel after the dust is removed by the dust collector 30.

なお、炉1内の銑鉄(溶融状態)Bが所定量に達する
と、出湯孔2をホールオープナーで開口して銑鉄Bおよ
び溶融スラグCを出湯する。出湯後は、マッドガンによ
り出湯孔2にマッドなどの閉塞材を詰め込んで、出湯孔
2を閉塞する。
When the amount of pig iron (molten state) B in the furnace 1 reaches a predetermined amount, the tap hole 2 is opened by a hole opener, and the pig iron B and the molten slag C are tapped. After tapping, the mud gun fills the tap hole 2 with a blocking material such as a mud to close the tap hole 2.

上記実施例では、溶鉄Aの注入前に窒素ガスを炉1内に
吹き込むが、これは注入容器11からの空気の侵入を防止
するために炉1の内圧を大気圧よりやや高くするのに行
うものであり、窒素ガスの吹き込み時間および量は僅か
である。
In the above-mentioned embodiment, nitrogen gas is blown into the furnace 1 before the molten iron A is injected, but this is performed to make the internal pressure of the furnace 1 slightly higher than the atmospheric pressure in order to prevent the invasion of air from the injection container 11. However, the blowing time and amount of nitrogen gas are short.

第2図は本考案の第2実施例にかかる溶融還元炉を示す
もので、本実施例の炉1aが上記実施例の炉1と相違する
ところは、溶融金属の注入部11aの構造が異なること、
および炉1a内への酸素の吹き込みをランス5を用いず、
吹き込みノズル16で行うようにしたことである。注入部
11aは、同図に示すように、上端を開放した漏斗状注入
器からなり、閉塞機構としてのレードルストッパー型ロ
ッド17を下降してその下端部を注入器11aの出口17′に
嵌入させることにより出口17′を閉塞し、ロッド17を上
昇することにより、出口17′を開放できるようになって
いる。その他の構成については、上記実施例との炉1と
共通するので、共通する部材については、第1図で使用
した符号を用いて第2図中に示し、説明を省略する。
FIG. 2 shows a smelting reduction furnace according to a second embodiment of the present invention. The difference between the furnace 1a of this embodiment and the furnace 1 of the above embodiment is the structure of the molten metal injection part 11a. thing,
And without using the lance 5 for blowing oxygen into the furnace 1a,
That is, the blowing nozzle 16 is used. Injection part
11a, as shown in the figure, consists of a funnel-shaped injector with an open upper end, and by lowering the ladle stopper type rod 17 as a closing mechanism and inserting the lower end into the outlet 17 'of the injector 11a. The outlet 17 'can be opened by closing the outlet 17' and raising the rod 17. Since other configurations are common to the furnace 1 of the above-described embodiment, common members are shown in FIG. 2 with the same reference numerals used in FIG. 1, and description thereof is omitted.

第2実施例の溶融還元炉1aにおいて、溶融金属Aの炉1a
内への注入は、次のようにして行われる。すなわち、ロ
ッド17で注入器11aの出口17′を閉塞した状態で、窒素
ガスを炉1a内に吹き込んで加圧すると共に、注入器11a
に所定量の溶融金属Aを注入する。そしてロッド17を上
昇して出口17′を開放し、種湯としての溶融金属Aを炉
1a内に注入する。このとき、出口17′は溶融金属Aで塞
がれており、また炉1a内の圧力が窒素ガスで大気圧以上
に加圧されているので、窒素ガスの一部が出口17′およ
び溶融金属A内から外部に排出されるが、炉1a内への空
気の侵入は確実に阻止される。こうして、注入器11a内
に溶融金属Aが残っている状態で、ロッド17を下降して
出口17′を閉塞すれば、炉1a内と外界(空気)との接触
を阻止して、溶融金属Aを炉1a内に注入できる。
In the smelting reduction furnace 1a of the second embodiment, the molten metal A furnace 1a
The injection into the inside is performed as follows. That is, with the rod 17 closing the outlet 17 'of the injector 11a, nitrogen gas is blown into the furnace 1a to pressurize it and the injector 11a
A predetermined amount of molten metal A is injected into. Then, the rod 17 is lifted to open the outlet 17 ', and the molten metal A as the seed water is heated in the furnace.
Inject into 1a. At this time, since the outlet 17 'is blocked by the molten metal A and the pressure in the furnace 1a is increased to the atmospheric pressure or higher by the nitrogen gas, a part of the nitrogen gas is discharged from the outlet 17' and the molten metal. Although it is discharged from the inside of A to the outside, invasion of air into the furnace 1a is surely prevented. Thus, when the molten metal A remains in the injector 11a and the rod 17 is lowered to close the outlet 17 ', contact between the inside of the furnace 1a and the outside (air) is prevented, and the molten metal A is blocked. Can be injected into the furnace 1a.

第3図は本考案の第3実施例にかかる溶融還元炉を示す
もので、本実施例の炉1bが上記第1実施例の炉1と相違
するところは、溶融金属Aの注入部11bの構造が異なる
こと、および炉口3と煙道4とをヘッド4′を介して接
続したことである。注入部11bは、同図に示すように、
上端開口に密閉蓋12を備えた漏斗状注入容器からなり、
この注入容器11bの出口は、略U字形のサイフォン式閉
塞管18を介して炉1bの注入孔8に接続されている。その
他の構成については、上記実施例の炉1と共通するの
で、共通する部材については、第1図で使用した符号を
用いて第3図中に示し、説明を省略する。
FIG. 3 shows a smelting reduction furnace according to a third embodiment of the present invention. The difference between the furnace 1b of this embodiment and the furnace 1 of the first embodiment is that the injection part 11b of the molten metal A is The structure is different, and the furnace port 3 and the flue 4 are connected via a head 4 '. The injection part 11b, as shown in the figure,
It consists of a funnel-shaped injection container with a closed lid 12 at the top opening,
The outlet of the injection container 11b is connected to the injection hole 8 of the furnace 1b through a siphon-type closed pipe 18 having a substantially U shape. Since other configurations are common to those of the furnace 1 of the above-mentioned embodiment, common members are shown in FIG. 3 by using the reference numerals used in FIG. 1, and description thereof is omitted.

第3実施例の溶融還元炉1bにおいて溶融金属の炉1b内へ
の注入は、窒素ガスを炉1b内に吹き込んで加圧し、密閉
蓋12を開放して注入容器11bに所定量の溶融金属Aを注
入する。注入された溶融金属Aは、サイフォン式閉塞管
18内を充たして、炉1b内と注入容器11b内とを遮断す
る。密閉蓋12を閉じた後、炉1b内の圧力を下げると、注
入容器11b内の溶融金属Aが炉1b内に注入される。この
とき、注入容器11bの上端開口は密閉蓋12で密閉され、
またその出口もサイフォン式閉塞管18内を充たした溶融
金属Aで塞がれているので、炉1b内への空気の侵入は確
実に阻止される。また、注入容器11b内の溶融金属Aが
全て注入されても、閉塞管18内を溶融金属Aが充たして
いるので、注入容器11bと炉1bとは常に遮断された状態
にある。
Injecting molten metal into the furnace 1b in the smelting reduction furnace 1b of the third embodiment, nitrogen gas is blown into the furnace 1b to pressurize it, the sealing lid 12 is opened, and a predetermined amount of molten metal A is injected into the injection container 11b. Inject. The injected molten metal A is a siphon-type closed tube.
The inside of the furnace 1b and the inside of the injection container 11b are shut off by filling the inside of the furnace 18. When the pressure in the furnace 1b is lowered after closing the sealing lid 12, the molten metal A in the injection container 11b is injected into the furnace 1b. At this time, the upper end opening of the injection container 11b is sealed with the sealing lid 12,
Further, since its outlet is also closed with the molten metal A filling the inside of the siphon type closed pipe 18, the invasion of air into the furnace 1b is surely prevented. Further, even if all the molten metal A in the injection container 11b is injected, the closed pipe 18 is filled with the molten metal A, so that the injection container 11b and the furnace 1b are always shut off.

第4図は本考案の第4実施例にかかる溶融還元炉1cで、
煙道4に注入孔8′を開設して溶融金属Aの注入器11c
を煙道4の注入孔8′に接続したところが、上記第2実
施例の炉1aと相違する。なお、図中における注入器11c
の出口側のバルブ部分(閉塞機構)17cは、実際には上
記第2実施例(第2図)で示したレードルストッパー型
ロッド17とこの先端部が嵌合する出口17′とを組み合わ
せたもの、あるいは第3実施例(第3図)で示したサイ
フォン式閉塞管18が用いられる。
FIG. 4 shows a smelting reduction furnace 1c according to a fourth embodiment of the present invention.
An injection hole 8'is formed in the flue 4 to inject the molten metal A into the injector 11c.
Is connected to the injection hole 8'of the flue 4, which is different from the furnace 1a of the second embodiment. The injector 11c in the figure
The valve portion (closure mechanism) 17c on the outlet side of is actually a combination of the ladle stopper type rod 17 shown in the second embodiment (FIG. 2) and the outlet 17 'to which this tip end fits. Alternatively, the siphon type closed tube 18 shown in the third embodiment (FIG. 3) is used.

第5図は本考案の第5実施例にかかる溶融還元炉1dを示
すものである。同図のように、本実施例では、漏斗状注
入器11dと炉1dの注入孔8との間に、溶融金属Aの貯留
タンク19をそれぞれ閉塞機構を介在させて介設してい
る。なお、図中のバルブ部分(閉塞機構)のうち上部側
17dは、第2実施例(第2図)で示したレードルストッ
パー型ロッド17とこの先端部が嵌合する出口17′とを組
み合わせたものが、また下部側18dは、第3実施例(第
3図)で示したサイフォン式閉塞管18がそれぞれ用いら
れる。
FIG. 5 shows a smelting reduction furnace 1d according to a fifth embodiment of the present invention. As shown in the figure, in this embodiment, a storage tank 19 for the molten metal A is provided between the funnel-shaped injector 11d and the injection hole 8 of the furnace 1d with a closing mechanism interposed therebetween. The upper part of the valve part (blocking mechanism) in the figure
17d is a combination of the ladle stopper type rod 17 shown in the second embodiment (Fig. 2) and the outlet 17 'into which this tip end fits, and the lower side 18d is the third embodiment (third embodiment). The siphon-type closed pipe 18 shown in FIG. 3) is used.

本実施例の溶融還元炉1dでは、貯留タンク19と注入孔8
との間のバルブ部分18dを閉じた状態で、注入器11dとの
間のバルブ部分17dを開放し、貯留タンク19内に窒素ガ
ス導入管14から高圧窒素ガスを吹き込んで空気をパージ
させた後、貯留タンク19内に漏斗状注入器11dから溶融
金属Aを注入する。そして注入器11d側のバルブ部分17d
を閉じ、注入孔7側のバルブ部分18dを開放して、貯留
タンク19内の溶融金属Aを炉1d内に注入する。したがっ
て、本実施例の溶融還元炉1dにおける種湯としての溶融
金属Aの炉1d内への注入は、外界と完全に遮断した状態
で行われる。
In the smelting reduction furnace 1d of this embodiment, the storage tank 19 and the injection hole 8
After closing the valve portion 18d between and, open the valve portion 17d between the injector 11d, after blowing high pressure nitrogen gas from the nitrogen gas introduction pipe 14 into the storage tank 19 to purge the air. The molten metal A is injected into the storage tank 19 from the funnel-shaped injector 11d. And the valve portion 17d on the injector 11d side
Is closed, the valve portion 18d on the injection hole 7 side is opened, and the molten metal A in the storage tank 19 is injected into the furnace 1d. Therefore, the molten metal A as the seed water in the smelting reduction furnace 1d of this embodiment is injected into the furnace 1d in a state of being completely cut off from the outside.

なお、溶融還元炉1と溶融金属の注入部11とを隔絶する
手段として、上記したロッド17(第2図)やサイフォン
式閉塞管18(第3図)の代わりに、マッドガン・ホール
オープナーによる開閉部を注入口8に設けてもよい。ま
た製鉄用の溶融還元に限らず、クロム鉱石からフェロク
ロムを得るなど、他の金属の溶融還元にも同様の溶融還
元炉を使用できる。
As a means for isolating the smelting reduction furnace 1 and the molten metal injection part 11, instead of the rod 17 (Fig. 2) and the siphon-type closed pipe 18 (Fig. 3), opening and closing by a mud gun hole opener. A part may be provided in the injection port 8. The same smelting reduction furnace can be used not only for smelting reduction for iron making but also for smelting reduction of other metals such as obtaining ferrochrome from chromium ore.

[考案の効果] 本考案の溶融還元炉によれば、次のような効果がもたら
される。
[Effects of the Invention] According to the smelting reduction furnace of the present invention, the following effects are brought about.

(1)炉を傾動させずに、溶融金属の注入および還元溶
融金属の出湯を可能にしたので、炉と煙道を接続するヘ
ッドを省いたり、あるいは従来の転炉型炉に用いられて
いたヘッドに比べてその構造を簡素化したりでき、また
炉の傾動装置が不要になるため、設備費の大幅な低減が
図れる。また、従来の炉と違って溶融金属(種湯)の注
入のたびに炉と煙道の接続を解く必要がないので、稼働
率も大幅に向上する。
(1) Since the molten metal can be injected and the reduced molten metal can be tapped without tilting the furnace, the head for connecting the furnace and the flue can be omitted, or the conventional converter furnace can be used. The structure can be simplified compared to the head, and the tilting device of the furnace is not required, so that the facility cost can be significantly reduced. Further, unlike the conventional furnace, it is not necessary to disconnect the furnace and the flue each time the molten metal (seed water) is injected, so the operation rate is greatly improved.

(2)上記(1)と同じ理由により、溶融金属の注入ご
とに煙道内の空気やガスをパージする必要がないので、
パージに必要な時間を短縮でき、稼働率を向上し得るう
えに、パージ用の多量の不活性ガスも要らなくなるの
で、経済的である。しかも、炉内および煙道内に空気が
混入しないので、溶融還元により炉内で発生する可燃成
分をもつ高温の還元ガスと空気中の酸素との接触による
急激な燃焼を確実に防止でき、作業の安全性も向上する
と共に、還元ガスの炉外への放出がほとんどなく、回収
率が向上するので、還元ガスを予備還元や燃料に有効に
利用できる。
(2) For the same reason as (1) above, it is not necessary to purge the air and gas in the flue every time the molten metal is injected,
It is economical because the time required for purging can be shortened, the operating rate can be improved, and a large amount of inert gas for purging is not required. Moreover, since air is not mixed in the furnace and the flue, it is possible to reliably prevent rapid combustion due to contact between high-temperature reducing gas having a combustible component generated in the furnace due to smelting reduction and oxygen in the air. The safety is improved, and the reducing gas is hardly released to the outside of the furnace, and the recovery rate is improved. Therefore, the reducing gas can be effectively used for preliminary reduction and fuel.

(3)請求項2記載の溶融還元炉によれば、炉と外界と
を完全に遮断した状態で、溶融金属を炉内へ注入するこ
とができる。
(3) According to the smelting reduction furnace of the second aspect, the molten metal can be injected into the furnace in a state where the furnace and the external environment are completely cut off.

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

第1図は本考案の溶融還元炉を備えた製鉄用の溶融還元
系統図である。第2図は本考案の第2実施例にかかる溶
融還元炉を示す断面図、第3図は本考案の第3実施例に
かかる溶融還元炉を示す断面図、第4図は本考案の第4
実施例にかかる溶融還元炉を示す断面図、第5図は本考
案の第5実施例にかかる溶融還元炉を示す断面図であ
る。第6図は従来の転炉型溶融還元炉を示す断面図であ
る。 1、1a、1b、1c、1d…溶融還元炉(固定型炉)、2…出
湯孔、3…炉口、4…煙道、5…ランス、8…注入孔、
11、11a、11b、11c、11d…注入部、12、17、18…閉塞機
構、19…貯留タンク。
FIG. 1 is a smelting reduction system diagram for iron making equipped with the smelting reduction furnace of the present invention. 2 is a sectional view showing a smelting reduction furnace according to a second embodiment of the present invention, FIG. 3 is a sectional view showing a smelting reduction furnace according to a third embodiment of the present invention, and FIG. 4 is a sectional view showing the present invention. Four
FIG. 5 is a sectional view showing a smelting reduction furnace according to an embodiment, and FIG. 5 is a sectional view showing a smelting reduction furnace according to a fifth embodiment of the present invention. FIG. 6 is a sectional view showing a conventional converter-type smelting reduction furnace. 1, 1a, 1b, 1c, 1d ... Smelting reduction furnace (fixed type furnace), 2 ... Tap hole, 3 ... Furnace opening, 4 ... Flue, 5 ... Lance, 8 ... Injection hole,
11, 11a, 11b, 11c, 11d ... Injection part, 12, 17, 18 ... Closure mechanism, 19 ... Storage tank.

───────────────────────────────────────────────────── フロントページの続き (72)考案者 矢島 健一 兵庫県神戸市中央区東川崎町3丁目1番1 号 川崎重工業株式会社神戸工場内 (72)考案者 滝浦 賢 兵庫県神戸市中央区東川崎町3丁目1番1 号 川崎重工業株式会社神戸工場内 (72)考案者 辰田 聡 兵庫県神戸市中央区東川崎町3丁目1番1 号 川崎重工業株式会社神戸工場内 (72)考案者 高座 幸彦 兵庫県神戸市中央区東川崎町3丁目1番1 号 川崎重工業株式会社神戸工場内 (72)考案者 佐藤 寿美男 兵庫県神戸市中央区東川崎町3丁目1番1 号 川崎重工業株式会社神戸工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Kenichi Yajima, 3-1, 1-1 Higashikawasaki-cho, Chuo-ku, Kobe-shi, Hyogo Prefecture Kawasaki Heavy Industries, Ltd. Kobe factory (72) Ken Ken Takiura Higashi-kawasaki, Chuo-ku, Kobe-shi, Hyogo 3-1-1, Kawasaki Heavy Industries, Ltd. Kobe factory (72) Inventor Satoshi Tatsuda 3-1-1, Higashikawasaki-cho, Chuo-ku, Kobe, Hyogo Prefecture 1-1, Kawasaki Heavy Industries Ltd. (72) Inventor, Yukihiko Takaza 3-1, 1-1 Higashikawasaki-cho, Chuo-ku, Kobe-shi, Hyogo Inside the Kawasaki Heavy Industries, Ltd. Kobe factory (72) Inventor: Sumio Sato 3-1-1, Higashi-kawasaki-cho, Chuo-ku, Kobe, Hyogo Prefecture Inside the Kobe factory, Kawasaki Heavy Industries, Ltd.

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】炉内の溶融金属浴中に、原料としての鉱石
を石炭などの副原料とともに装入し、酸素を吹き込んで
溶融状態で還元させるための金属浴炉式の溶融還元炉で
あって、 前記炉の炉口に煙道を直接又はヘッドを介して接続し、 該炉の底部に開閉可能な出湯孔を設け、 前記炉の上部又は煙道に溶融金属の注入孔を開設し、 該注入孔に溶融金属の注入部を接続すると共に、注入孔
と注入部との間に又は注入部の受入れ口に閉塞機構を設
けたことを特徴とする溶融還元炉。
1. A metal-bath furnace type smelting reduction furnace for charging ore as a raw material together with an auxiliary raw material such as coal into a molten metal bath in the furnace, and blowing oxygen into the molten metal for reduction in a molten state. A flue is connected to the furnace mouth of the furnace directly or through a head, a tap hole that can be opened and closed is provided at the bottom of the furnace, and a molten metal injection hole is opened at the top of the furnace or the flue. A smelting reduction furnace characterized in that a molten metal injection part is connected to the injection hole, and a closing mechanism is provided between the injection hole and the injection part or at a receiving port of the injection part.
【請求項2】前記注入孔と前記注入部との間に、それぞ
れ閉塞機構を介在して溶融金属の貯留タンクを介設し、
該貯留タンクに高圧の不活性ガスの導入管を接続した請
求項1記載の溶融還元炉。
2. A molten metal storage tank is provided between the injection hole and the injection portion with a closing mechanism interposed therebetween.
The smelting reduction furnace according to claim 1, wherein a high-pressure inert gas introduction pipe is connected to the storage tank.
JP7031290U 1990-06-29 1990-06-29 Smelting reduction furnace Expired - Fee Related JPH0754281Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7031290U JPH0754281Y2 (en) 1990-06-29 1990-06-29 Smelting reduction furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7031290U JPH0754281Y2 (en) 1990-06-29 1990-06-29 Smelting reduction furnace

Publications (2)

Publication Number Publication Date
JPH0429646U JPH0429646U (en) 1992-03-10
JPH0754281Y2 true JPH0754281Y2 (en) 1995-12-18

Family

ID=31606366

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7031290U Expired - Fee Related JPH0754281Y2 (en) 1990-06-29 1990-06-29 Smelting reduction furnace

Country Status (1)

Country Link
JP (1) JPH0754281Y2 (en)

Also Published As

Publication number Publication date
JPH0429646U (en) 1992-03-10

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