JPH0196313A - Smelting reduction method - Google Patents
Smelting reduction methodInfo
- Publication number
- JPH0196313A JPH0196313A JP25248187A JP25248187A JPH0196313A JP H0196313 A JPH0196313 A JP H0196313A JP 25248187 A JP25248187 A JP 25248187A JP 25248187 A JP25248187 A JP 25248187A JP H0196313 A JPH0196313 A JP H0196313A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- iron ore
- gas
- smelting
- charged
- 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.)
- Granted
Links
- 238000003723 Smelting Methods 0.000 title claims abstract description 42
- 238000000034 method Methods 0.000 title claims abstract description 25
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 85
- 229910052742 iron Inorganic materials 0.000 claims abstract description 41
- 239000007789 gas Substances 0.000 claims abstract description 27
- 239000002893 slag Substances 0.000 claims abstract description 22
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 19
- 239000001301 oxygen Substances 0.000 claims abstract description 19
- 239000000463 material Substances 0.000 claims abstract description 11
- 238000002485 combustion reaction Methods 0.000 claims abstract description 7
- 239000011261 inert gas Substances 0.000 claims abstract description 5
- 239000003575 carbonaceous material Substances 0.000 claims description 21
- 239000002184 metal Substances 0.000 claims description 10
- 229910052751 metal Inorganic materials 0.000 claims description 10
- 238000005261 decarburization Methods 0.000 claims description 5
- 238000002844 melting Methods 0.000 claims description 3
- 230000008018 melting Effects 0.000 claims description 3
- 239000000567 combustion gas Substances 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 239000002994 raw material Substances 0.000 abstract description 18
- 238000003756 stirring Methods 0.000 abstract description 8
- 238000007664 blowing Methods 0.000 abstract description 5
- 230000003628 erosive effect Effects 0.000 abstract description 2
- 238000005262 decarbonization Methods 0.000 abstract 1
- 238000006722 reduction reaction Methods 0.000 description 19
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 239000012159 carrier gas Substances 0.000 description 3
- 229910001882 dioxygen Inorganic materials 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
Landscapes
- Manufacture Of Iron (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は炭材を燃料および還元材として用い、鉄鉱石
を転炉型製錬炉内において溶融状態で還元する溶融還元
法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a smelting reduction method in which iron ore is reduced in a molten state in a converter-type smelting furnace using carbonaceous materials as fuel and reducing material.
[従来の技術]
溶融還元法は、高炉製銑法に変わるものであり、高炉製
銑法においては高炉の建設費が高く、広大な敷地が必要
であるという高炉製銑法の欠点を解消すべく、近年に至
り開発されたものである。[Conventional technology] The smelting reduction method is an alternative to the blast furnace iron making method, and it eliminates the drawbacks of the blast furnace iron making method, such as the high construction cost and the need for a large site. It has been developed in recent years.
この還元法においては、製錬炉内の溶銑中に鉄鉱石又は
予備還元された鉄鉱石が装入され、また還元材または燃
料となる炭材及び石灰その他の造滓材を装入された製錬
炉内に酸素が吹き込まれる。In this reduction method, iron ore or pre-reduced iron ore is charged into hot metal in a smelting furnace, and carbonaceous materials, lime and other slag materials are charged as reducing agents or fuel. Oxygen is blown into the furnace.
そうすると炭材が溶銑中に溶解するとともに、炭材のC
が酸素ガスによって酸化される。このときの酸化熱によ
って鉄鉱石が溶融されるとともに、鉄鉱石が炭材中のC
によって還元される。溶銑から発生するCOガスは過剰
に吹き込まれる酸素ガスにより2次燃焼されてC02ガ
スになる。このCO2ガスの顕熱は、溶銑上を覆ってい
るスラグ及びフォーミンク状の粒鉄に伝達され、次いで
溶銑に伝達される。Then, the carbonaceous material is dissolved in the hot metal, and the carbonaceous material is dissolved in the hot metal.
is oxidized by oxygen gas. The iron ore is melted by the oxidation heat at this time, and the iron ore is
will be reduced by The CO gas generated from the hot metal is subjected to secondary combustion by the excessively blown oxygen gas and becomes CO2 gas. The sensible heat of this CO2 gas is transferred to the slag and foamed iron particles covering the hot metal, and then to the hot metal.
こうして鉄鉱石が還元されて溶銑が製造されるが、製錬
炉内の鉄鉱石の還元°反応の促進をはかって、前記鉄鉱
石又は炭材を前記製錬炉の側壁または炉底に設けた羽口
からキャリアーガスとともに装入する方法が提案されて
いる。(特開昭58−14407、特開昭60−145
307 )[発明が解決しようとする問題点]
しかしながら、製錬炉の側壁または炉底の羽口からキャ
リヤガスを用いて鉄鉱石又は炭材を吹き込む方法におい
ては羽口の溶損及び摩耗が激しく、また鉄鉱石または炭
材の吹込量を多くするにはキャリヤガスを増加しなけれ
ばならないが、そうすると吹抜けの現象が生じて鉄鉱石
または炭材がスラグもしくは溶銑の中に止どまる歩留り
が悪くなる。In this way, the iron ore is reduced to produce hot metal, but in order to promote the reduction reaction of the iron ore in the smelting furnace, the iron ore or carbon material is provided on the side wall or bottom of the smelting furnace. A method of charging together with carrier gas through the tuyere has been proposed. (JP-A-58-14407, JP-A-60-145
307) [Problems to be Solved by the Invention] However, in the method of injecting iron ore or carbonaceous material from the tuyere on the side wall or bottom of the smelting furnace using a carrier gas, the tuyeres are subject to severe erosion and wear. In addition, in order to increase the amount of iron ore or carbonaceous material injected, it is necessary to increase the carrier gas, but this causes a phenomenon of blow-through, resulting in poor yields in which the iron ore or carbonaceous material remains in the slag or hot metal. Become.
また、酸素ランスのノズルまたは前記羽口から原料を吹
き込む場合、吹き込まれた原料が製錬炉内に均一に混合
されるまでに時間がかかり反応が遅くなるおそれがある
。さらに、炭材を酸素ランスから吹き込む場合、炉内の
反応が不均一となり、スラグ中の鉄含有量(T−Fe)
の高い部分が形成されて炉内のスラグが飛散される所謂
スロッピングが生じるという問題があった。Further, when the raw material is blown into the nozzle of the oxygen lance or the tuyere, it takes time for the blown raw material to be uniformly mixed in the smelting furnace, and the reaction may be slow. Furthermore, when carbonaceous material is injected through an oxygen lance, the reaction inside the furnace becomes uneven, and the iron content (T-Fe) in the slag decreases.
There is a problem in that a high area is formed and the slag in the furnace is scattered, resulting in so-called slopping.
この発明は、かかる問題点を解決するためになされたも
のであって、炉壁または炉底の羽口の溶損もしくは損耗
を抑えて、鉄鉱石の還元蓮度の促進を図るとともにスロ
ツビンクーの発生を低減させる溶融還元法を提供しよう
とするものである。This invention was made to solve these problems, and aims to promote the degree of reduction of iron ore by suppressing the melting or wear of the tuyere on the furnace wall or the bottom of the furnace, and the generation of slothbinku. The purpose of the present invention is to provide a melt reduction method that reduces the
[問題点を解決するための手段及び作用]この発明によ
る溶融還元法は製錬炉内の鉄浴に炭材と酸素を加え、予
熱予備還元炉で予熱、予備還元された鉄鉱石を前記製錬
炉に装入して溶融還元により溶銑な製造する方法におい
て、酸素は脱炭用及び2次燃焼用ノズルを有する上吹き
酸素ランスから吹込まれ、不活性ガスまたは製錬炉で発
生するガスが炉体側壁及び炉底壁に設けられた羽口から
吹き込まれるとともに、鉄鉱石、炭材及び造滓材は全て
前記製錬炉の上方から投下されることを特徴とする。[Means and effects for solving the problems] The smelting reduction method according to the present invention adds carbonaceous material and oxygen to an iron bath in a smelting furnace, and preheats and prereduced iron ore in a preheating and prereducing furnace. In the method of producing hot metal by charging it into a smelting furnace and reducing it by smelting, oxygen is blown through a top-blown oxygen lance that has decarburization and secondary combustion nozzles, and inert gas or gas generated in the smelting furnace is blown into it. The smelting furnace is characterized in that the iron ore, carbonaceous materials, and slag materials are all blown into the furnace from the tuyeres provided on the side walls and the bottom wall of the furnace, and are dropped from above the smelting furnace.
鉄鉱石、炭材、石灰等は全て前記炉体の上方に設けられ
た装入用ホッパーから炉内に投下され、炉体の側壁及び
炉底に設けられた羽目から吹き込まれたガスは製錬炉内
の鉄浴またはスラグ層を撹拌する。こうすると炉内にお
いて鉄鉱石、炭材、石灰等は均一に混合される時間が短
縮されて鉄鉱石の還元反応が促進され、スロッピングの
発生頻度の低減および羽口の寿命延長により操業の安定
と製造コストの低減を図ることが出来る。Iron ore, carbonaceous materials, lime, etc. are all dropped into the furnace from a charging hopper installed above the furnace body, and the gas blown through the slats installed on the side walls and bottom of the furnace body is used for smelting. Stir the iron bath or slag layer in the furnace. This shortens the time for the iron ore, carbonaceous material, lime, etc. to be uniformly mixed in the furnace, promoting the reduction reaction of the iron ore, and stabilizing operations by reducing the frequency of slopping and extending the life of the tuyeres. This makes it possible to reduce manufacturing costs.
炉内に投下する方法としてスラグ面上に均一に投下する
かまたは炉底羽口からのガス吹込により盛り上がった浴
面上に向けて集中的に投下することが鉄鉱石、炭材、石
灰等の均一混合に対してより一層効果的である。The method of dropping iron ore, carbonaceous materials, lime, etc. into the furnace is to uniformly drop it onto the slag surface, or to dump it concentratedly onto the bath surface which is raised by blowing gas from the bottom tuyere. It is much more effective for uniform mixing.
[実施例] 本発明の実施例を添付の図面を参照しながら説明する。[Example] Embodiments of the invention will be described with reference to the accompanying drawings.
第1図は本発明の溶融還元法に用いられるプロセスの説
明図である。製錬炉10内には鉄v611及びスラグ層
12が形成され、副原料である炭材及び造滓材が装入さ
れる第1のシュー ト13が前記fRPJ炉炉の上部に
設けられている。前記第1のシュート13はその下部が
炉頂付近に設けられた貫通口15に遊貫され、その上部
にはフレキシブルジヨイント16で特に図示していない
装入用ホッパーに連結されている。FIG. 1 is an explanatory diagram of the process used in the melt reduction method of the present invention. Iron V611 and a slag layer 12 are formed in the smelting furnace 10, and a first chute 13 into which carbon material and slag material as auxiliary materials are charged is provided at the top of the fRPJ furnace. . The lower part of the first chute 13 is loosely inserted into a through hole 15 provided near the top of the furnace, and the upper part thereof is connected to a charging hopper (not shown) by a flexible joint 16.
また酸素を吹き込む酸素ランス21が炉内に鉛直に挿入
されている。前記ランスには脱炭用酸素及び2次燃焼用
酸素を噴出する、ノズル22.23が夫々設けられてい
る。第1図で酸素ランス21の先端に示した矢印は28
.29は夫々脱炭用、2次燃焼用の酸素の吹きだし方向
を示す。前記炉の上方には流動層型の反応、装置である
予熱予備還元炉30が設けられ、これに第2のシュート
31から鉄鉱石が供給され、ここで予熱、予備還元され
た鉄鉱石は第3のシュート32から前記製錬炉10に挿
入される。前記第3のシュート31は第1のシュートと
同様に貫通口35に遊貫され、フレキシブルジヨイント
36を有している。Further, an oxygen lance 21 for blowing oxygen is inserted vertically into the furnace. The lances are provided with nozzles 22 and 23, respectively, for injecting oxygen for decarburization and oxygen for secondary combustion. The arrow shown at the tip of the oxygen lance 21 in Figure 1 is 28
.. 29 indicates the direction in which oxygen is blown out for decarburization and for secondary combustion, respectively. A preheating and pre-reducing furnace 30, which is a fluidized bed type reaction device, is provided above the furnace, and iron ore is supplied to this from a second chute 31, and the iron ore that has been preheated and pre-reduced here is passed through the second chute. It is inserted into the smelting furnace 10 through the chute 32 of No. 3. Like the first chute, the third chute 31 is loosely inserted into the through hole 35 and has a flexible joint 36.
予熱予備還元炉30に製錬炉10の発生ガスを供給する
導管33が設けられ、また、予熱予備還元炉30の排ガ
スからダストを除去するホットサイクロン37、予熱予
備還元炉30の排出ガスの顕熱を利用して蒸気を得る熱
交換器38が設けられている。さらに、前記製錬炉10
の側壁及び炉底には攪拌用のガスを吹き込む羽口25.
26が夫々設けられている。A conduit 33 for supplying gas generated from the smelting furnace 10 to the preheating pre-reduction furnace 30 is provided, and a hot cyclone 37 for removing dust from the exhaust gas from the preheating pre-reduction furnace 30 and a conduit 33 for removing dust from the exhaust gas from the preheating pre-reduction furnace 30 are provided. A heat exchanger 38 is provided to obtain steam using heat. Furthermore, the smelting furnace 10
There are tuyeres 25 on the side walls and bottom of the furnace for blowing gas for stirring.
26 are provided respectively.
なお、原料事情、設備費用、操業の容易性等を考慮して
予熱予備還元炉として、熱効率の良いシャフト炉型、も
しくは設備費用が低減されまた操業が容易であるロータ
リキルン型のものを設けることは本発明の実施にあたっ
て全く支障はない。In addition, in consideration of raw material conditions, equipment costs, ease of operation, etc., a shaft furnace type with good thermal efficiency or a rotary kiln type with reduced equipment costs and easy operation should be installed as the preheating pre-reduction furnace. There is no problem at all in carrying out the present invention.
以上ののように構成された溶融還元装置の作用について
説明する。鉄鉱石は第2のシュート31から予熱予備還
元炉30装入にされここで製錬炉10から導管33を通
して発生ガスの供給を受けて予熱および還元された後、
製錬炉10に第2のシュート81を通して装入される。The operation of the melting reduction apparatus configured as above will be explained. The iron ore is charged from the second chute 31 to the preheating pre-reduction furnace 30, where it is supplied with generated gas from the smelting furnace 10 through the conduit 33, and is preheated and reduced.
It is charged into the smelting furnace 10 through the second chute 81.
副原料である炭材、造滓材は装入装置が簡便である通常
の装入用ホッパー(図示せず)から第1のシュート13
を通して製錬炉10内に装入される。第1、第8のシュ
ート13.33は夫々貫通口15.35に遊貫され、フ
レキシブルジヨイント16.36を有しているので、そ
れぞれ主原料、副原料の投下方向を製錬炉10の、浴面
上の炉底羽口から吹き込まれる撹拌ガスによる盛り上が
り部分に調整することができる。従って主前記原料、副
原料は全て前記浴面上の撹拌ガスによる盛り上がり部分
に集中的に投下される。Carbon material and slag material, which are auxiliary raw materials, are transferred from a normal charging hopper (not shown) with a simple charging device to a first chute 13.
The smelting furnace 10 is charged through the smelting furnace 10. The first and eighth chutes 13.33 are each loosely penetrated through the through hole 15.35 and have a flexible joint 16.36, so that the direction in which the main raw material and auxiliary raw material are thrown is directed to the smelting furnace 10. , it can be adjusted to the raised area due to the stirring gas blown in from the bottom tuyere above the bath surface. Therefore, the main raw material and the auxiliary raw material are all concentratedly dropped onto the bulge formed by the stirring gas on the bath surface.
製錬炉内に上記のように盛り上がり部分に集中的に投下
されて装入された主原料及び副原料は、製錬炉の側壁及
び炉底に設けられた羽口25.26から吹き込まれる撹
拌用ガスによって撹拌され、既に炉内に形成されている
鉄浴またはスラグ層の中にすみやかに均一に混合される
。この撹拌用ガスはAr、N2等の不活性ガスまたは前
記予熱予備還元炉からの排ガス即ちプロセスガスが用い
られる。一方前記酸素ランス21の脱炭用及び2次燃焼
用ノズル22.23から供給される酸素は前記炭材を酸
化させて原料である鉄鉱石を還元するのに十分な熱源を
供給する。The main raw materials and auxiliary raw materials charged into the smelting furnace by being intensively dropped into the swelled portion as described above are stirred by being blown into the tuyeres 25 and 26 provided on the side wall and bottom of the smelting furnace. The slag gas is stirred by the slag gas and quickly and uniformly mixed into the iron bath or slag layer already formed in the furnace. As this stirring gas, an inert gas such as Ar or N2 or an exhaust gas from the preheating pre-reduction furnace, that is, a process gas is used. On the other hand, oxygen supplied from the decarburization and secondary combustion nozzles 22 and 23 of the oxygen lance 21 provides a heat source sufficient to oxidize the carbonaceous material and reduce the iron ore that is the raw material.
第1表はスラグ中に含まれるFeの含有量である(T−
Fe)及びスロッピングについて本発明と従来例につい
て夫々比較したものである。Table 1 shows the content of Fe contained in the slag (T-
This figure compares the present invention and a conventional example with respect to Fe) and slopping.
(T−Fe)が本発明の方法により低下していることは
鉄鉱石の還元反応が促進されていることを示すものであ
り、また本発明の方法によりスロッピングの発生頻度が
明かに減少していることが示されている。第1表でスロ
ッピング割合は製錬中のスロッピングの生じた時間と製
錬時間の割合である。The fact that (T-Fe) is reduced by the method of the present invention indicates that the reduction reaction of iron ore is promoted, and the frequency of occurrence of slopping is clearly reduced by the method of the present invention. It has been shown that In Table 1, the slopping ratio is the ratio of the time during smelting when slopping occurred and the smelting time.
第1表
[1発明の効果]
本発明によれば製錬炉の側壁及び炉底に設けられた羽目
から酸素ガスは吹き込まれず、撹拌ガスとして不活性ま
たはプロセスガスが吹き込まれ、原料はすべて前記製錬
炉の上方から前記炉底がらの撹拌ガスによる浴面の盛り
上がり部分に向けて集中的に投入されるので、装入され
た原料は速に炉内で均一に混合されて鉄鉱石の還元反応
が促進され、スロッピングの発生頻度の低減及び羽口寿
命延長により操業の安定と製造コストの低減を図ること
が出来る。Table 1 [1 Effects of the Invention] According to the present invention, oxygen gas is not blown into the side walls and bottom of the smelting furnace, but an inert or process gas is blown in as the stirring gas, and all the raw materials are Since the raw materials are intensively charged from the top of the smelting furnace toward the swollen part of the bath surface created by the stirring gas from the bottom of the furnace, the charged raw materials are quickly and uniformly mixed in the furnace and the iron ore is reduced. The reaction is promoted, the frequency of slopping is reduced, and the life of the tuyere is extended, which leads to stable operations and reduced manufacturing costs.
第1図は本発明の溶融還元法に用いられるプロセスの説
明図である。
10・・・製錬炉、11・・・鉄浴、12・・・スラグ
層、13・・・第1のシュート、15.
35・・・貫通口、16,36・・・フレキシブルジョ
イン ト 、 2 1 ・・・ 酸 素
ラ ン ス 、22.23、・・・ノズル、30
・・・予熱予備還元炉、3 1 ・・・ 第 2
の シ ュ − ト 、32・・・
第3のシュート、33・・・導管、37・・・ホットサ
イクロン、38・・・蒸気発生器。
特許出願人 日本銅管株式会社FIG. 1 is an explanatory diagram of the process used in the melt reduction method of the present invention. 10... Smelting furnace, 11... Iron bath, 12... Slag layer, 13... First chute, 15. 35...Through hole, 16,36...Flexible joint, 21...Oxygen
Lance, 22.23,... Nozzle, 30
... Preheating preliminary reduction furnace, 3 1 ... 2nd
Shoot, 32...
Third chute, 33... Conduit, 37... Hot cyclone, 38... Steam generator. Patent applicant Nippon Doppan Co., Ltd.
Claims (3)
元炉で予熱、予備還元された鉄鉱石を前記製錬炉に装入
して溶融還元により溶銑を製造する方法において、酸素
は脱炭用及び2次燃焼用ノズルを有する上吹き酸素ラン
スから吹込まれ、不活性ガスまたは製錬炉で発生するガ
スが炉体側壁及び炉底壁に設けられた羽口から吹き込ま
れるとともに、鉄鉱石、炭材及び造滓材は全て前記製錬
炉の上方から投下されることを特徴とする溶融還元法。(1) In a method in which carbonaceous material and oxygen are added to an iron bath in a smelting furnace, and iron ore that has been preheated and prereduced in a preheating prereduction furnace is charged into the smelting furnace to produce hot metal by smelting reduction. Oxygen is blown in from a top-blown oxygen lance that has nozzles for decarburization and secondary combustion, and inert gas or gas generated in the smelting furnace is blown in through tuyeres provided on the side wall and bottom wall of the furnace body. Also, a smelting reduction method characterized in that iron ore, carbonaceous materials, and slag materials are all dropped from above the smelting furnace.
からのガス吹込により盛り上がった浴面に向けて集中的
に投下されることを特徴とする特許請求の範囲第1項に
記載の溶融還元法。(2) The iron ore, carbonaceous material, and slag material are intensively dropped toward the bath surface which is raised by gas injection from the tuyere on the bottom wall of the furnace. Melting reduction method described in Section.
に投下されることを特徴とする特許請求の範囲第1項に
記載の溶融還元法。(3) The smelting reduction method according to claim 1, wherein the iron ore, carbonaceous material, and slag material are uniformly dropped onto the upper surface of the slag.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62252481A JP2638840B2 (en) | 1987-10-08 | 1987-10-08 | Smelting reduction method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62252481A JP2638840B2 (en) | 1987-10-08 | 1987-10-08 | Smelting reduction method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0196313A true JPH0196313A (en) | 1989-04-14 |
JP2638840B2 JP2638840B2 (en) | 1997-08-06 |
Family
ID=17237978
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62252481A Expired - Fee Related JP2638840B2 (en) | 1987-10-08 | 1987-10-08 | Smelting reduction method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2638840B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0387308A (en) * | 1989-08-29 | 1991-04-12 | Nippon Steel Corp | Method for operating iron bath reaction vessel |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6164807A (en) * | 1984-09-03 | 1986-04-03 | Nippon Steel Corp | Melt reduction method of iron ore |
JPS62192513A (en) * | 1986-02-17 | 1987-08-24 | Nippon Kokan Kk <Nkk> | Method and apparatus for melt reduction |
JPS62228410A (en) * | 1986-03-31 | 1987-10-07 | Kawasaki Steel Corp | Method for recovering metal from granular ore by melt reduction |
-
1987
- 1987-10-08 JP JP62252481A patent/JP2638840B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6164807A (en) * | 1984-09-03 | 1986-04-03 | Nippon Steel Corp | Melt reduction method of iron ore |
JPS62192513A (en) * | 1986-02-17 | 1987-08-24 | Nippon Kokan Kk <Nkk> | Method and apparatus for melt reduction |
JPS62228410A (en) * | 1986-03-31 | 1987-10-07 | Kawasaki Steel Corp | Method for recovering metal from granular ore by melt reduction |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0387308A (en) * | 1989-08-29 | 1991-04-12 | Nippon Steel Corp | Method for operating iron bath reaction vessel |
Also Published As
Publication number | Publication date |
---|---|
JP2638840B2 (en) | 1997-08-06 |
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