JPH0141919B2 - - Google Patents
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- Publication number
- JPH0141919B2 JPH0141919B2 JP56045831A JP4583181A JPH0141919B2 JP H0141919 B2 JPH0141919 B2 JP H0141919B2 JP 56045831 A JP56045831 A JP 56045831A JP 4583181 A JP4583181 A JP 4583181A JP H0141919 B2 JPH0141919 B2 JP H0141919B2
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- Prior art keywords
- iron ore
- gas
- metallurgical furnace
- furnace
- charging
- 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.)
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- Manufacture And Refinement Of Metals (AREA)
- Manufacture Of Iron (AREA)
- Furnace Details (AREA)
Description
【発明の詳細な説明】
本発明は、冶金炉から出るガスを利用して、冶
金炉内に投入される冶金炉装入用鉄鉱石を加熱還
元するための炉に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a furnace for heating and reducing iron ore for charging into a metallurgical furnace using gas emitted from the metallurgical furnace.
製鉄業は、先ず高炉にて鉄鉱石をコークスで還
元して溶銑を作り、次にこれを冶金炉に注入し、
その冶金炉内に酸素を吹き込んで(以下吹錬とい
う。)鋼を作る。 In the steel industry, iron ore is first reduced with coke in a blast furnace to produce hot metal, which is then injected into a metallurgical furnace.
Steel is made by blowing oxygen into the metallurgical furnace (hereinafter referred to as blowing).
この製鉄業において、鉄鉱石を還元するのに大
量のコークスが消費され(例えば鉄鉱石1ton当り
400〜500Kgのコークスを消費する。)、製鉄業にお
けるエネルギ消費の大半を占めている。 In this steel industry, a large amount of coke is consumed to reduce iron ore (for example, per ton of iron ore,
Consumes 400-500Kg of coke. ), which accounts for most of the energy consumption in the steel industry.
又、冶金炉内で吹錬を行い良質の鋼を作る際、
精錬中の熱バランス上冷却材として、冶金炉内に
鉄鉱石が装入される。 Also, when producing high quality steel by blowing in a metallurgical furnace,
Iron ore is charged into the metallurgical furnace as a coolant for heat balance during smelting.
一方、吹錬中に、冶金炉から高温の還元性ガス
が発生し、このガスは排ガス処理装置の冷却器で
熱回収された後、更に湿式除塵器で直接冷却さ
れ、900〜1000℃のガスの保有熱が無駄に放散さ
れてしまつているのが一般的である。 On the other hand, during blowing, high-temperature reducing gas is generated from the metallurgical furnace, and after this gas is heat recovered in the cooler of the exhaust gas treatment equipment, it is further cooled directly in the wet dust remover, and the gas reaches a temperature of 900 to 1000℃. Generally, the heat retained in the engine is wasted and dissipated.
本発明者等は、製鉄業の省エネルギ化を総合的
に考え、これまで無駄に放熱されていた冶金炉か
らのガスの保有熱を有効に利用して、冶金炉に冷
却材として装入されていた鉄鉱石を排ガスによつ
て加熱還元し、高炉での鉄鉱石の処理量を減少さ
せ、製鉄業の総合的な省エネルギ化を計るように
考究したものである。 The inventors of the present invention have comprehensively considered energy conservation in the steel industry, and have made effective use of the retained heat of the gas from the metallurgical furnace, which had been wasted in the past. The idea was to reduce the amount of iron ore processed in the blast furnace by heating and reducing the iron ore that had been previously used in the blast furnace, thereby achieving overall energy savings in the steel industry.
即ち、第1図に示すように、本発明は冶金炉1
で発生した高温の排ガスを、先ず冷却器2で熱回
収し、冷却器2を出た900〜1000℃の排ガスを第
1湿式集塵器3によつて直接水をかけ、温度を下
げた後、更に第2集塵器によつて降温除塵し、放
散塔6から放散するか又はホルダ7に回収してい
たこれまでの排ガス処理装置に、冶金炉装入用鉄
鉱石の加熱還元炉8を設け、第1湿式集塵器3に
入る前の排ガスの一部を送風機8′により鉄鉱石
の加熱還元炉8に導き、鉄鉱石を加熱還元し、冶
金炉内に装入するようにしたものである。尚、加
熱還元炉8の出口側ガスダクトを、第1集塵器ス
ロート部の出口側に接続し、送風機8′を省略す
ることもできる。即ち、本発明は、ルーバなどで
形成される通気性のある収容体に鉄鉱石を収容し
てある厚さのほぼ垂直な鉄鉱石層を形成し、この
層にほぼ直交するように風函及び又は仕切り部材
によりガス通路を複数形成し、前記鉄鉱石の層の
下端の鉄鉱石出口側に設けたガス入口から排ガス
を導入して、順次ガス通路を通過させ、鉄鉱石の
層の上端の入口側に設けたガス出口から加熱還元
炉8外へガスを排出させて、該鉄鉱石入口側から
前記ガス通路毎に鉄鉱石の温度を順次昇温させ、
この昇温と共に還元反応を促進させ、鉄鉱石の層
の出口側では、鉄鉱石を最も高温ならしめ且つ還
元反応を活発に行わせ、ほぼ所要の程度に還元さ
れたのち、排ガスの前記各通路に装填されている
量の鉄鉱石分ずつ冶金炉の間歇運転に合せて断続
的に取り出し、冶金炉へ直接装入するようにし、
冶金炉の間歇運転に対処するようにしたことを特
徴とするものである。 That is, as shown in FIG.
First, heat is recovered from the high-temperature exhaust gas generated in the cooler 2, and the exhaust gas at a temperature of 900 to 1000 degrees Celsius exiting the cooler 2 is directly sprayed with water through the first wet dust collector 3 to lower the temperature. In addition, a heating reduction furnace 8 for iron ore to be charged into a metallurgical furnace has been added to the conventional exhaust gas treatment equipment in which the temperature is lowered and dust removed by a second dust collector, and the iron ore is dissipated from a dispersion tower 6 or collected in a holder 7. A part of the exhaust gas before entering the first wet precipitator 3 is guided to an iron ore heating reduction furnace 8 by a blower 8' to heat and reduce the iron ore and charge it into the metallurgical furnace. It is. It is also possible to connect the outlet side gas duct of the heating reduction furnace 8 to the outlet side of the first dust collector throat portion and omit the blower 8'. That is, in the present invention, iron ore is accommodated in an air-permeable container formed by a louver or the like to form a thick, almost vertical iron ore layer, and a wind box and a Alternatively, a plurality of gas passages are formed using a partition member, and the exhaust gas is introduced from the gas inlet provided at the iron ore outlet side at the lower end of the iron ore layer, and is passed through the gas passages sequentially, and the exhaust gas is introduced from the gas inlet provided at the iron ore outlet side at the lower end of the iron ore layer. Gas is discharged to the outside of the heating reduction furnace 8 from a gas outlet provided on the side, and the temperature of the iron ore is sequentially raised in each of the gas passages from the iron ore inlet side,
As the temperature rises, the reduction reaction is promoted, and at the exit side of the iron ore layer, the iron ore is brought to the highest temperature and the reduction reaction is actively carried out, and after being reduced to almost the required degree, the exhaust gas is passed through each of the passages. The amount of iron ore loaded in the metallurgical furnace is taken out intermittently in accordance with the intermittent operation of the metallurgical furnace, and charged directly into the metallurgical furnace.
The present invention is characterized in that it is adapted to cope with intermittent operation of a metallurgical furnace.
以下、本発明による冶金炉装入用鉄鉱石の加熱
還元炉の一実施例を第2図によつて詳述すると、
傾斜角度45゜〜60゜としたルーバ9をある間隔に配
設し、通気性をもつた収容体を形成し、この通気
性をもつた収容体内に、鉄鉱石10を装填して、
ほぼ垂直な一つの鉄鉱石10の層を形成してい
る。このように装填された鉄鉱石10は、ルーバ
9の巾とピツチPを適正にすることによつて、ル
ーバ9のピツチPの間に溜つた鉄鉱石10の表面
が安息角となり、上層部と下層部での装填密度を
均一にし、ルーバ9のピツチPから外にこぼれ出
ることなく、通気性をもつた収容体の中に収容さ
れている。又、この鉄鉱石10の層の出口16に
は、カツトオフゲート17が設けられて、シリン
ダ18によつて開閉できるようになつており、鉄
鉱石10を層内から取り出せるようになつてい
る。11はガス入口部で、層の下方の鉄鉱石出口
16附近に設けられ、風函13,14によつて鉄
鉱石10の層をほぼ直角に横切るようにガス通路
を形成している。一方、ガスの出口12は、鉄鉱
石10の層の入口15附近に設けられている。本
実施例の場合のガス通路は、A,B,Cの3通路
となつている。尚、19はシールゲートで、非吹
錬時に加熱還元炉8内に空気が入らないようにな
つている。 Hereinafter, an embodiment of the heating reduction furnace for iron ore for charging into a metallurgical furnace according to the present invention will be described in detail with reference to FIG. 2.
Louvers 9 with an inclination angle of 45° to 60° are arranged at certain intervals to form a breathable container, and iron ore 10 is loaded into the breathable container.
One almost vertical layer of iron ore 10 is formed. By making the width and pitch P of the louver 9 appropriate, the iron ore 10 loaded in this way has an angle of repose between the surface of the iron ore 10 accumulated between the pitch P of the louver 9, and the upper layer The packing density in the lower layer is made uniform, and the louver 9 is housed in a ventilated container without spilling out from the pitch P of the louver 9. A cut-off gate 17 is provided at the outlet 16 of the layer of iron ore 10 and can be opened and closed by a cylinder 18, so that the iron ore 10 can be taken out from within the layer. Reference numeral 11 denotes a gas inlet section, which is provided near the iron ore outlet 16 below the layer, and a gas passage is formed by wind boxes 13 and 14 so as to cross the layer of iron ore 10 at a nearly right angle. On the other hand, the gas outlet 12 is provided near the inlet 15 of the layer of iron ore 10. In this embodiment, there are three gas passages A, B, and C. Note that 19 is a seal gate that prevents air from entering the heating reduction furnace 8 during non-blowing.
第3図は本発明の加熱還元炉の他の実施例で、
鉄鉱石10の層を円筒形としたもので、風函1
3′,14′及び仕切り部材23,24により、前
述の実施例と同様A,B,C3つのガス通路を形
成している。尚、21はガス出口、17′はカツ
トオフゲートである。 FIG. 3 shows another embodiment of the heating reduction furnace of the present invention,
A cylindrical layer of iron ore 10.
3', 14' and the partition members 23, 24 form three gas passages A, B, and C, as in the previous embodiment. In addition, 21 is a gas outlet, and 17' is a cut-off gate.
第4図はさらに本発明の加熱還元炉の他の実施
例で、鉄鉱石10の層のみを示したもので、ガス
通路毎にカツトオフゲート22を設けたものであ
る。尚、Hは鉄鉱石10の層の厚さである。 FIG. 4 shows another embodiment of the thermal reduction furnace of the present invention, showing only the layer of iron ore 10, and in which a cut-off gate 22 is provided for each gas passage. Note that H is the thickness of the layer of iron ore 10.
以上のように構成された本発明による冶金炉装
入用鉄鉱石の加熱還元炉の作用を説明する。 The operation of the iron ore heating reduction furnace for charging into a metallurgical furnace according to the present invention constructed as described above will be explained.
鉄鉱石10の層の厚さH、この鉄鉱石10の層
を通過するガス通路の数は、冶金炉の精錬処理能
力に応じて決定される。 The thickness H of the layer of iron ore 10 and the number of gas passages passing through the layer of iron ore 10 are determined depending on the refining processing capacity of the metallurgical furnace.
先ず、カツトオフゲート17,17′を閉の状
態にして鉄鉱石10を入口15から加熱還元炉8
内に装填し、鉄鉱石10の層を形成する。本実施
例の場合ガス通路の数は、A,B,Cの3つであ
る。この場合、ガス入口から入つた吹錬中の高温
ガスは、最初に鉄鉱石10の出口16に近いガス
通路C部の鉄鉱石10を加熱し、次にガス通路B
部の鉄鉱石10を、次いでガス通路A部の鉄鉱石
10を加熱して、ガス出口12から出る。このよ
うにガス通路C(鉄鉱石出口附近)を最も高い温
度に、次にガス通路B、次いでガス通路Aの順に
鉄鉱石10の温度は昇温される。 First, with the cutoff gates 17 and 17' closed, the iron ore 10 is transferred from the inlet 15 to the heating reduction furnace 8.
to form a layer of iron ore 10. In this embodiment, the number of gas passages is three, A, B, and C. In this case, the high-temperature gas entering from the gas inlet during blowing first heats the iron ore 10 in the gas passage C section near the outlet 16 of the iron ore 10, and then heats the iron ore 10 in the gas passage B
Then, the iron ore 10 in the gas passage A section is heated, and then the iron ore 10 in the gas passage A section is heated, and the iron ore 10 exits from the gas outlet 12. In this way, the temperature of the iron ore 10 is raised in the order of gas passage C (near the iron ore outlet) to the highest temperature, then gas passage B, and then gas passage A.
この3つのガス通路は、冶金炉の精錬処理能力
に合せて決定されたものとして説明すると、間歇
的に操業される冶金炉において、先ず始動時は三
回目の冶金炉の操業で、ガス通路Cの部分の鉄鉱
石10が丁度規定温度で、ほぼ所要の程度に還元
されるようになつている。この三回目の冶金炉操
業の後、カツトオフゲート17,17′を開け、
ガス通路Cの部分に装填されている規定温度に昇
温され且つ還元された鉄鉱石10を取り出し、カ
ツトオフゲート17,17′を閉じる。この時、
ガス通路Bに位置していた鉄鉱石10は、ガス通
路Cの所に、ガス通路Aに位置していた鉄鉱石1
0は、ガス通路Bに移動し、ガス通路Aには新し
く鉄鉱石10が装填される。前記のガス通路Cに
移動してきた鉄鉱石10は、すでに冶金炉操業の
二回目に等しい温度に昇温されていると共に還元
されており、冶金炉の四回目の操業で規定温度に
昇温され且つ還元される。この四回目の冶金炉操
業終了後、カツトオフゲート17,17′を開に
し、同様にガス通路Cの部分の鉄鉱石10を取り
出す。これと同時にガス通路Bの位置にある鉄鉱
石10はガス通路Cに、ガス通路Aの位置にある
鉄鉱石10はガス通路Bに、ガス通路Aには新た
に鉄鉱石10が装填される。 These three gas passages are determined according to the refining processing capacity of the metallurgical furnace.In a metallurgical furnace that is operated intermittently, when the metallurgical furnace is started for the third time, the gas passage C is The iron ore 10 in the area is reduced to approximately the required degree at exactly the specified temperature. After this third metallurgical furnace operation, the cut-off gates 17, 17' are opened,
The iron ore 10 that has been heated to a specified temperature and reduced, which is charged in the gas passage C, is taken out, and the cut-off gates 17 and 17' are closed. At this time,
The iron ore 10 located in gas passage B is replaced by the iron ore 1 located in gas passage A in gas passage C.
0 moves to the gas passage B, and the gas passage A is newly loaded with iron ore 10. The iron ore 10 that has been moved to the gas passage C has already been heated to the same temperature and reduced in the second operation of the metallurgical furnace, and is heated to the specified temperature in the fourth operation of the metallurgical furnace. And it will be returned. After the fourth metallurgical furnace operation is completed, the cut-off gates 17, 17' are opened and the iron ore 10 in the gas passage C is similarly taken out. At the same time, the iron ore 10 located in the gas passage B is loaded into the gas passage C, the iron ore 10 located in the gas passage A is loaded into the gas passage B, and a new iron ore 10 is loaded into the gas passage A.
このように連続的に鉄鉱石10は規定温度に昇
温され且つ還元され、冶金炉内に各操業毎に投入
される。特に第4図に示すように、各ガス通路毎
にカツトオフゲート22を設け、出口側のカツト
オフゲート22から順次開閉していくことによつ
て、鉄鉱石10はガス通路毎に完全に区切られた
状態で移動することができる。 In this way, the iron ore 10 is continuously heated to a specified temperature and reduced, and then introduced into the metallurgical furnace for each operation. In particular, as shown in FIG. 4, by providing a cut-off gate 22 for each gas passage and sequentially opening and closing the cut-off gate 22 from the outlet side, the iron ore 10 is completely separated for each gas passage. It is possible to move in a closed state.
以上詳述した通り本発明の冶金炉装入用鉄鉱石
の加熱還元炉は、通気性のある収容体に冶金炉装
入用鉄鉱石を装填して、冶金炉装入用鉄鉱石の層
を形成し、この層をほぼ直角に横切るガス通路を
複数設け、該層の冶金炉装入用鉄鉱石の出口側か
らガスを通すようにし、1つのガス通路内に装填
されている冶金炉装入用鉄鉱石の量だけ取り出す
ようにしたので、ガス入口側から出口側に向つて
順次冶金炉装入用鉄鉱石を昇温し、還元反応を促
進させ、ガス入口通路に装填されている冶金炉装
入用鉄鉱石を、ガス通路の数の分だけ、ガスと接
触して加熱還元し、ガス通路の数を冶金炉の操業
に合せて決めることにより、間歇的に発生するガ
ス及び温度とCO濃度が変化しても、ほぼ均一に
冶金炉装入用鉄鉱石を加熱還元することができ
る。 As described above in detail, the heating reduction furnace for iron ore for metallurgical furnace charging of the present invention loads iron ore for metallurgical furnace charging into an air-permeable container and forms a layer of iron ore for metallurgical furnace charging. A metallurgical furnace charge in which a plurality of gas passages are formed and cross this layer at approximately right angles, and gas is passed from the outlet side of the iron ore for metallurgical furnace charging in the layer, and the metallurgical furnace charge is charged in one gas passage. Since only the amount of iron ore for metallurgical furnace charging is taken out, the temperature of the iron ore for metallurgical furnace charging is raised sequentially from the gas inlet side to the outlet side to promote the reduction reaction, and the metallurgical furnace charged in the gas inlet passage is heated. Iron ore for charging is heated and reduced by contacting with gas for the number of gas passages, and by determining the number of gas passages according to the operation of the metallurgical furnace, it is possible to reduce the intermittent gas, temperature, and CO2. Even if the concentration changes, iron ore for charging into a metallurgical furnace can be heated and reduced almost uniformly.
更に一定温度の冶金炉装入用鉄鉱石を得ること
により、冶金炉内での熱バランスと炉内反応への
影響をなくすことができ、間歇的に発生し且つ温
度とCO濃度が一定でないガスを有効に利用し、
製鉄業における総合的な省エネルギ化が計れる等
その効果は大である。 Furthermore, by obtaining iron ore for charging into a metallurgical furnace at a constant temperature, it is possible to eliminate the effect on the heat balance and reactions within the metallurgical furnace, and to eliminate gases that occur intermittently and whose temperature and CO concentration are not constant. make effective use of
The effects are significant, including the ability to achieve comprehensive energy savings in the steel industry.
また本発明の冶金炉装入用鉄鉱石の加熱還元炉
は、冶金炉の排ガス処理装置の除塵器の上流側よ
り排ガスを分岐導入するように構成したので、排
ガス主通路内に集塵層を兼ねた鉄鉱石や焼結用ペ
レツトの充填層を設けて加熱還元を行う方式に比
べて、集塵を目的としないため、冶金炉装入用鉄
鉱石の粒度の選択幅が広く、且つ層厚も自由に選
択できる他、既設の排ガス処理設備の大規模な改
造を要することなく設置可能であり、設備コスト
が著しく安くなるという利点がある。 In addition, the thermal reduction furnace for iron ore charging in a metallurgical furnace of the present invention is configured so that the exhaust gas is branched in from the upstream side of the dust remover of the exhaust gas treatment device of the metallurgical furnace, so that a dust collection layer is formed in the exhaust gas main passage. Compared to a method that performs thermal reduction using a packed bed of iron ore or pellets for sintering, since the purpose is not to collect dust, there is a wide range of particle sizes to choose from for the iron ore charged in the metallurgical furnace, and the layer thickness is In addition to being freely selectable, it can be installed without requiring large-scale modification of existing exhaust gas treatment equipment, which has the advantage of significantly reducing equipment costs.
第1図は従来の排ガス処理装置に本発明の冶金
炉装入用鉄鉱石の加熱還元炉を適用した全体説明
図、第2図乃至第4図は本発明の加熱還元炉の実
施例で、第2図は冶金炉装入用鉄鉱石が平板状の
場合、第3図は円筒状の場合、第4図はガス流路
毎にカツトオフゲートを設けた場合である。
8,8′……加熱還元炉、9……ルーバ、10
……冶金炉装入用鉄鉱石、11……ガス入口、1
2……ガス出口、13,13′,14,14′……
風函、15……鉄鉱石入口、16……鉄鉱石出
口、17,17′,22……カツトオフゲート、
23……仕切り部材。
FIG. 1 is an overall explanatory diagram of the heat-reduction furnace for iron ore for metallurgical furnace charging of the present invention applied to a conventional exhaust gas treatment device, and FIGS. 2 to 4 show examples of the heat-reduction furnace of the present invention. Fig. 2 shows the case where the iron ore for charging the metallurgical furnace is in the form of a flat plate, Fig. 3 shows the case in the case where it is cylindrical, and Fig. 4 shows the case where a cut-off gate is provided for each gas flow path. 8, 8'... Heating reduction furnace, 9... Louver, 10
...Iron ore for charging metallurgical furnace, 11 ...Gas inlet, 1
2... Gas outlet, 13, 13', 14, 14'...
Fukan, 15...Iron ore entrance, 16...Iron ore exit, 17, 17', 22...Cut-off gate,
23...Partition member.
Claims (1)
は放散する排ガス回収装置の除塵器の上流側より
分岐した排ガスバイパス流路の途中に設けられ高
温の還元性ガスを導入して利用する冶金炉装入用
鉄鉱石の加熱還元炉であつて、鉄鉱石を収容して
ほぼ垂直な鉄鉱石の層を形成するためのルーバな
どで形成された通気可能な収容体と、上記鉄鉱石
層をほぼ直交するように複数のガス通路を形成す
るための風函及び又は仕切り部材とが設けられ、
前記収容体の上端には鉄鉱石入口が備えられ、前
記収容体の下部には鉄鉱石を冶金炉へ装入するた
めの出口が備えられ、且つ鉄鉱石の出口側に冶金
炉から出るガスを分岐導入するガス入口が設けら
れ、鉄鉱石の入口側に該ガスを排出するガス出口
が設けられていることを特徴とする冶金炉装入用
鉄鉱石の加熱還元炉。1. A metallurgical furnace that is installed in the middle of an exhaust gas bypass channel that branches from the upstream side of the dust remover of an exhaust gas recovery device that cools and removes dust from the gas emitted from the metallurgical furnace, and then collects or dissipates the gas, and uses the high-temperature reducing gas introduced therein. This is a heating reduction furnace for iron ore for charging, which includes a ventilable container formed of a louver or the like for storing iron ore and forming a nearly vertical layer of iron ore, and a container for storing iron ore to form a nearly vertical layer of iron ore. A wind box and/or partition member for forming a plurality of gas passages orthogonally is provided,
The upper end of the container is equipped with an iron ore inlet, the lower part of the container is equipped with an outlet for charging iron ore into the metallurgical furnace, and the iron ore outlet side is equipped with an iron ore inlet for charging iron ore into the metallurgical furnace. 1. A thermal reduction furnace for iron ore for charging into a metallurgical furnace, characterized in that a gas inlet is provided for introducing the gas in a branched manner, and a gas outlet for discharging the gas is provided on the inlet side of the iron ore.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4583181A JPS57161483A (en) | 1981-03-28 | 1981-03-28 | Heat reduction furnace for iron ore |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4583181A JPS57161483A (en) | 1981-03-28 | 1981-03-28 | Heat reduction furnace for iron ore |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57161483A JPS57161483A (en) | 1982-10-05 |
| JPH0141919B2 true JPH0141919B2 (en) | 1989-09-08 |
Family
ID=12730169
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4583181A Granted JPS57161483A (en) | 1981-03-28 | 1981-03-28 | Heat reduction furnace for iron ore |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57161483A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6070000U (en) * | 1983-10-21 | 1985-05-17 | 大同特殊鋼株式会社 | Bucket for charging steelmaking raw materials |
| JP5446505B2 (en) * | 2009-06-26 | 2014-03-19 | Jfeスチール株式会社 | Melting reduction method |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5396905A (en) * | 1977-02-04 | 1978-08-24 | Kawasaki Heavy Ind Ltd | Method and exhaust gas from converter accompanied by gasification of coal |
| JPS5749784A (en) * | 1980-09-08 | 1982-03-23 | Kawasaki Heavy Ind Ltd | Exhaust gas treatment apparatus for metallurgical furnace equipped with device for heating or heat reducing charge |
| JPS57126908A (en) * | 1981-01-31 | 1982-08-06 | Nippon Steel Corp | Purification of exhaust gas from uncombustion-type converter furnace |
-
1981
- 1981-03-28 JP JP4583181A patent/JPS57161483A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57161483A (en) | 1982-10-05 |
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