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JPH0826378B2 - Method for producing molten iron containing chromium - Google Patents

Method for producing molten iron containing chromium

Info

Publication number
JPH0826378B2
JPH0826378B2 JP61259418A JP25941886A JPH0826378B2 JP H0826378 B2 JPH0826378 B2 JP H0826378B2 JP 61259418 A JP61259418 A JP 61259418A JP 25941886 A JP25941886 A JP 25941886A JP H0826378 B2 JPH0826378 B2 JP H0826378B2
Authority
JP
Japan
Prior art keywords
chromium
fuel
slag
coke
coal
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 - Lifetime
Application number
JP61259418A
Other languages
Japanese (ja)
Other versions
JPS63111108A (en
Inventor
信 深川
輝久 下田
稔 石川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP61259418A priority Critical patent/JPH0826378B2/en
Publication of JPS63111108A publication Critical patent/JPS63111108A/en
Publication of JPH0826378B2 publication Critical patent/JPH0826378B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/10Reduction of greenhouse gas [GHG] emissions
    • Y02P10/143Reduction of greenhouse gas [GHG] emissions of methane [CH4]

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  • Manufacture Of Iron (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 この発明は上下吹転炉等の溶融還元炉においてクロム
鉱石、クロム鉱石の予備処理品を石炭、コークス等の炭
素源により溶融還元してステンレス鋼を製造する際のク
ロム含有量が39%以下のクロム含有溶鉄の製造方法に関
する。
TECHNICAL FIELD The present invention relates to a smelting reduction furnace such as an up-down blow converter to melt-reduce chromium ore and a pretreated product of chromium ore with a carbon source such as coal or coke to produce stainless steel. The present invention relates to a method for producing molten iron containing chromium having a chromium content of 39% or less during production.

従来技術とその問題点 従来、ステンレス鋼の製造はクロム鉱石等を電気炉に
て炭素還元して製造したフエロクロムを用いて溶製され
てきた。しかしこの方法では、高価な電力を用いるこ
と、フエロクロムをいったん凝固させ、製鋼過程で再溶
融するのでエネルギー損失が大きい等の理由により、フ
エロクロムのコストが高くつき、結果的にステンレス鋼
のコストアップを予儀なくされていた。
Conventional technology and its problems Conventionally, stainless steel has been produced by melting chromium ore and the like in an electric furnace using ferrochrome produced by carbon reduction. However, in this method, the cost of ferrochrome is high due to the use of expensive electric power and the large energy loss because the ferrochrome is once solidified and remelted in the steelmaking process, resulting in a cost increase of stainless steel. It was rude.

このような問題点を解決するため、例えば、クロム鉱
石またはその予備処理品を上下吹転炉等の溶融還元炉で
電力を使わずにコークス等を用いて炭素還元してフエロ
クロムを溶製しステンレス鋼を製造する方法、すなわち
クロム鉱石の溶融還元法(特開昭54-158320号等)が試
みられている。
In order to solve such a problem, for example, chromium ore or a pretreated product thereof is carbon-reduced with coke or the like in a smelting reduction furnace such as a vertical blowing converter without using electric power to melt ferrochrome to produce stainless steel. A method for producing steel, that is, a smelting reduction method for chromium ores (Japanese Patent Laid-Open No. 54-158320, etc.) has been attempted.

クロム鉱石の溶融還元法は、クロム鉱石を溶融スラグ
中に溶解しCr酸化物およびFe酸化物を含有したスラグを
形成せしめ、溶湯中の[C]や石炭、コークス等の炭材
により還元することにより、クロム含有溶鉄を製造する
ことを基本原理とするものである。
The smelting reduction method of chrome ore is to dissolve chrome ore in molten slag to form slag containing Cr oxide and Fe oxide, and reduce with [C] in the molten metal or carbonaceous material such as coal or coke. According to the above, the basic principle is to produce molten iron containing chromium.

すなわち、下記反応が進行する。 That is, the following reaction proceeds.

(Cr2O3)+3C=2Cr+3CO (FeO)+C=Fe+CO 上記反応は大きな吸熱反応である。従って、クロム鉱
石を溶融還元するためには熱供給の手段をこうじる必要
があり、そのため石炭、コークス等の燃料を酸素や空気
により燃焼させる方法が種々試みられている。
(Cr 2 O 3 ) + 3C = 2 Cr + 3CO (FeO) + C = Fe + CO The above reaction is a large endothermic reaction. Therefore, in order to smelt and reduce chromium ore, it is necessary to twist the means of heat supply, and therefore various methods of burning fuel such as coal and coke with oxygen and air have been tried.

クロム鉱石の溶融還元の場合、多量のスラグが発生す
ること、並びにそのスラグとメタルまたは炭材との界面
が還元反応界面であるため、多量のスラグ存在下でかつ
還元反応を妨げないように燃料を燃焼させる必要があ
る。その方法として、メタル浴中に石炭粉やコークス粉
等の炭素質固体と酸素・空気等の酸化性ガスを吹込み燃
焼させる方法(特開昭58-100656号)、並びにスラグ浴
上にコークス等の炭材を浮かべ燃焼させる方法(特開昭
59-140349号)が知られている。
In the case of smelting reduction of chromium ore, a large amount of slag is generated, and the interface between the slag and the metal or carbonaceous material is the reduction reaction interface. Need to be burned. As the method, a carbonaceous solid such as coal powder and coke powder and an oxidizing gas such as oxygen and air are blown into a metal bath and burned (JP-A-58-100656), as well as coke on a slag bath. Method of floating burning carbonaceous material
59-140349) is known.

特開昭58-100656号の方法では、吹込んだ炭材は大部
分COまでしか燃焼しない。吹込み羽口近傍ではCO2まで
完全燃焼させたとしても、CO2が直ちに溶銑中の[C]
と反応し、COガスになってしまうからである。
In the method disclosed in JP-A-58-100656, most of the injected carbonaceous material burns up to CO. Even in the blowing tuyeres near was completely burned to CO 2, CO 2 immediately in hot metal [C]
It reacts with and becomes CO gas.

一方、特開昭59-140349の方法でも、浮遊しているコ
ークス等の炭材がCO2ガスと直ちに反応しCOガスとなる
ため、大部分COガスまでしか燃焼しない。
On the other hand, according to the method disclosed in JP-A-59-140349, the carbonaceous material such as coke floating in the reactor immediately reacts with CO 2 gas to form CO gas, so that most of it burns up to CO gas.

つまり、いずれの方法も燃料を部分酸化(不完全燃
焼)することにより熱供給を行なっているものの、それ
だけでは発熱量が少なく、そのため多量の燃料や酸素を
消費することを予儀なくされる。
In other words, in each of the methods, the heat is supplied by partially oxidizing the fuel (incomplete combustion), but the amount of heat generated is small by itself, and therefore it is inevitable to consume a large amount of fuel and oxygen.

ちなみに、Cの燃料を例にとると、部分酸化の場合と
完全燃焼の場合でその燃焼量が大きく異なる。
By the way, in the case of the C fuel as an example, the combustion amount is greatly different between the partial oxidation and the complete combustion.

クロム鉱石の溶融還元法において、その燃料並びに酸
素原単位を大幅に低減するため、還元反応を妨げること
なく燃料を完全燃焼させ、かつスラグ・メタル浴に有効
に伝熱する方法が開発されれば、その生産性、経済性を
飛躍的に向上させることができ、その方法の開発が待た
れていた。
In the smelting reduction method of chromium ore, if a method of completely burning the fuel without hindering the reduction reaction and effectively transferring heat to the slag / metal bath in order to greatly reduce the fuel and oxygen unit consumption is to be developed. , Its productivity and economic efficiency can be dramatically improved, and the development of the method has been awaited.

発明の目的 この発明は従来の前記問題点を解決するためになされ
たもので、クロム鉱石の溶融還元時多量に存在するスラ
グ浴中に炭素および水素を主成分とする燃料と酸素を燃
料がほぼ完全燃焼するような比率で吹込むことにより、
燃料をほぼ完全燃焼させ、スラグ浴を効率よく加熱し、
かつスラグ−メタル界面でクロム鉱石由来のクロム酸化
物並びに鉄酸化物を迅速に還元するため、メタル浴中に
石炭、コークス等の還元剤を吹込むことを特徴とするク
ロム含有溶鉄の製造方法を提案せんとするものである。
OBJECT OF THE INVENTION The present invention has been made to solve the above-mentioned problems of the related art, and in a slag bath which is present in a large amount during the smelting reduction of chromium ore, a fuel containing carbon and hydrogen as the main components and oxygen are almost used as fuel. By blowing in a ratio that will burn completely,
Burns fuel almost completely, efficiently heats the slag bath,
Moreover, in order to rapidly reduce chromium oxide and iron oxide derived from chromium ore at the slag-metal interface, a method for producing chromium-containing molten iron, characterized in that a reducing agent such as coal or coke is blown into the metal bath. It is a proposal.

発明の構成 この発明に係るクロム含有溶鉄の製造方法は、クロム
鉱石、クロム鉱石を前処理して製造した未還元クロムペ
レット,半還元クロムペレット,クロム焼結鉱等を石
炭、コークス等の炭素源により溶融還元してクロム含有
量が39%以下のクロム含有溶鉄を製造するに際し、スラ
グ浴内に炭素および水素を主成分とする燃料と酸素を燃
料がほぼ完全燃焼するような比率で吹込むことにより、
燃料を燃焼させスラグ浴を加熱するとともに金属浴中に
石炭、コークス等の還元剤を吹込み[C]濃度を3%以
上に保つことを特徴とするものである。
Configuration of the Invention A method for producing molten iron containing chromium according to the present invention is a method for producing a chromium ore, an unreduced chromium pellet produced by pretreating a chromium ore, a semi-reduced chromium pellet, a chromium sintered ore, etc. as a carbon source such as coal or coke. When producing molten iron containing chromium with a chromium content of 39% or less by smelting and reducing with, blow a fuel containing carbon and hydrogen as the main components and oxygen in a ratio so that the fuel burns almost completely in the slag bath. Due to
It is characterized in that the fuel is burned to heat the slag bath, and a reducing agent such as coal or coke is blown into the metal bath to keep the [C] concentration at 3% or more.

すなわち、この発明はスラグ浴中に燃料と酸素を吹込
むことにより、燃料の完全燃焼を可能とし、かつその燃
焼熱を容易にスラグ浴に伝熱せしめる方法である。
That is, the present invention is a method for injecting fuel and oxygen into the slag bath to enable complete combustion of the fuel and to easily transfer the heat of combustion to the slag bath.

なお、この発明においてクロム含有量を39%以下に限
定しているのは、本プロセスはステンレス鋼溶製のため
のクロム含有母溶湯を製造することを目的としており、
Cr濃度を40%以上に上げる必要がないからである。
In the present invention, the chromium content is limited to 39% or less, the purpose of this process is to produce a chromium-containing mother molten metal for melting stainless steel,
This is because it is not necessary to raise the Cr concentration to 40% or more.

以下、この発明方法について詳細に説明する。 Hereinafter, the method of the present invention will be described in detail.

この発明者らは、クロム鉱石、またはその予備処理品
を溶融還元してクロム含有溶鉄を製造する方法における
熱効率向上対策(燃焼並びに酸素消費量低減対策)につ
いて種々検討した結果、溶融還元処理において、スラグ
中に石炭、コークス等の燃料と酸素を燃料がほぼ完全燃
焼するような比率で吹込むことにより燃料をほぼ完全燃
焼させることができ、かつ有効にスラグ浴に伝熱し得る
ことを見い出した。
As a result of various studies on the thermal efficiency improvement measures (combustion and oxygen consumption reduction measures) in the method of producing chromium-containing molten iron by smelting reduction of chromium ore or its pretreatment product, the present inventors It has been found that the fuel such as coal and coke and oxygen can be blown into the slag at a ratio such that the fuel is almost completely burned, so that the fuel can be almost completely burned and the heat can be effectively transferred to the slag bath.

次に、スラグ中吹込みによる燃料完全燃焼条件下にお
いて、クロム鉱石の溶融還元反応速度を調査したとこ
ろ、基本的にスラグ−メタル間での還元反応速度に影響
をおよぼさないことが判明した。これは、吹込み燃料の
燃焼帯がスラグ浴内でスラグ−メタル界面よりかなり上
の部分にあるため、燃焼により発生したCO2ガスはスラ
グ浴内を上昇するもののスラグ−メタル界面には到達せ
ず、生成したメタルを再酸化するような還元反応を妨げ
る作用を生じないためである。しかし、スラグ−メタル
間還元反応によりメタル中の[C]は消費され、還元進
行にともないメタル中[C]濃度が低下していくが、
[C]濃度が3%以下になると還元反応速度が著しく低
下することが実験により判明した。従って、何等かの手
段でメタル浴中にCを添加し、[C]濃度を3%以上に
保つ工夫が必要である。反応器上部より石炭、コークス
等の還元剤を添加したのでは、スラグ浴に妨げられてメ
タル中に加炭できない上、スラグ中で完全燃焼し発生し
たCO2ガスが還元剤と反応してCOに戻ってしまう。
Next, when the smelting reduction reaction rate of chromium ore was investigated under the condition of complete combustion of fuel by blowing into the slag, it was found that it basically does not affect the reduction reaction rate between the slag and the metal. . This is because the combustion zone of the injected fuel is in the slag bath well above the slag-metal interface, so the CO 2 gas generated by combustion rises in the slag bath but does not reach the slag-metal interface. This is because there is no action of interfering with the reduction reaction such as reoxidation of the produced metal. However, [C] in the metal is consumed by the reduction reaction between the slag and the metal, and the [C] concentration in the metal decreases as the reduction progresses.
It was found from an experiment that the reduction reaction rate was significantly reduced when the [C] concentration was 3% or less. Therefore, it is necessary to add C to the metal bath by some means to keep the [C] concentration at 3% or more. If a reducing agent such as coal or coke is added from the upper part of the reactor, it cannot be carburized in the metal because it is hindered by the slag bath, and the CO 2 gas generated by complete combustion in the slag reacts with the reducing agent to generate CO. Will return to.

そこで、種々検討した結果、メタル浴中に石炭、コー
クス等還元剤を吹込むことにより、スラグ浴中で燃料を
完全燃焼させる条件下でもメタル浴中への加炭が容易に
でき、[C]濃度を3%以上に保つことによりクロム鉱
石の溶融還元反応を迅速に完了させることを見出したの
である。
Therefore, as a result of various studies, by blowing a reducing agent such as coal or coke into the metal bath, it is possible to easily carburize the metal bath even under the condition that the fuel is completely burned in the slag bath, and [C] It was found that the smelting reduction reaction of chromium ore can be completed rapidly by keeping the concentration at 3% or more.

この発明は上記の知見に基づいてなされたものであ
り、クロム鉱石等を溶融還元してクロム含有溶鉄を製造
するに際し、スラグ浴内に炭素および水素を主成分とす
る燃料と酸素を燃料がほぼ完全燃焼するような比率で吹
込むことにより、燃料を完全燃焼させスラグ浴を効率よ
く加熱するとともに、金属浴中に石炭、コークス等の還
元剤を吹込み[C]濃度を3%以上に保つことにより溶
融還元反応を迅速に進行させることを特徴とするもので
ある。
The present invention was made based on the above findings, and when producing molten iron containing chromium by smelting and reducing chromium ore, a fuel containing carbon and hydrogen as the main components and oxygen as the fuel are almost always contained in the slag bath. Blows at a rate that completely burns to completely burn the fuel and efficiently heat the slag bath, and blow a reducing agent such as coal or coke into the metal bath to keep the [C] concentration at 3% or more. This is characterized in that the smelting reduction reaction proceeds rapidly.

なお、スラグ中に吹込む燃料としては、石炭,コーク
ス等の固体燃料、石油,タール等の液体燃料の他、メタ
ン,天然ガス等の気体燃料等が挙げられる。
Examples of the fuel blown into the slag include solid fuels such as coal and coke, liquid fuels such as petroleum and tar, and gas fuels such as methane and natural gas.

次にこの発明方法を図面に基づいて説明する。 Next, the method of the present invention will be described with reference to the drawings.

第1図はこの発明方法を実施するための装置を示す概
略図である。図中(1)は金属浴を貯える転炉型反応容
器であって、内部には金属浴(2)(例えば溶銑または
溶鋼)が収容されている。(3)はスラグ層である。
(4)は燃料および酸素吹込み用横吹羽口であり、還元
に必要な熱量はこの羽口での燃焼熱により供給され
る。、(5)は炭材吹込用底吹羽口であり、スラグ−メ
タル界面の還元反応に必要な炭素源が供給される。
FIG. 1 is a schematic view showing an apparatus for carrying out the method of the present invention. In the figure, (1) is a converter-type reaction vessel for storing a metal bath, and the metal bath (2) (for example, molten pig iron or molten steel) is housed inside. (3) is a slag layer.
Reference numeral (4) is a lateral tuyeres for blowing in fuel and oxygen, and the amount of heat required for reduction is supplied by the combustion heat at the tuyeres. , (5) are bottom blowers for blowing carbonaceous material, to which a carbon source necessary for the reduction reaction at the slag-metal interface is supplied.

本発明においては基本的に還元に必要な熱量はすべて
スラグ層内の燃料の完全燃焼により供給される。しか
し、より燃料の炉内での完全燃焼を確実にするためCOガ
スの助燃用O2をスラグ層の上方に設置したCO燃焼用上吹
ランス(6)、CO燃焼用横吹羽口(7)より供給するこ
とも可能である。
In the present invention, basically, the amount of heat required for the reduction is supplied by the complete combustion of the fuel in the slag layer. However, in order to ensure the complete combustion of fuel in the furnace, CO 2 combustion assisting O 2 was installed above the slag layer for CO combustion top blow lance (6) and CO combustion side blower tuyere (7). It is also possible to supply more.

なお、燃料および酸素吹込み用横吹羽口(4)は、例
えば中心管よりN2+コークス粉(石炭粉)を、中心管と
外管との間よりO2を、外管より冷却ガス(N2,C3H8等)
を吹込む構造の三重管羽口を用いることができる。クロ
ム鉱石、造滓剤(石炭石,珪石等)、原料は反応容器の
上部から炉内に投入される。
The side blower mouth (4) for injecting fuel and oxygen has, for example, N 2 + coke powder (coal powder) from the central tube, O 2 from between the central tube and the outer tube, and cooling gas (from the outer tube ( N 2 , C 3 H 8 etc.)
It is possible to use a triple tube tuyere having a structure of blowing air. Chromium ore, slag forming agents (coal stone, silica stone, etc.) and raw materials are charged into the furnace from the upper part of the reaction vessel.

以下に、この発明の実施例を示す。 Hereinafter, examples of the present invention will be described.

実施例1 第1図に示す反応容器と同一構造の10トン上底吹き転
炉を用い、第1表に示す条件でクロム鉱石の溶融還元を
行なった結果を、スラグ中に塊コークスを浮遊させその
炭材を燃焼させつつ還元を進行させる従来法と比較して
第2表に示す。
Example 1 The results of smelting reduction of chromium ore under the conditions shown in Table 1 using a 10-ton top-bottom blowing converter having the same structure as the reaction vessel shown in FIG. 1 were obtained by suspending lump coke in slag. Table 2 shows the comparison with the conventional method in which the reduction is advanced while burning the carbonaceous material.

第2表より明らかなごとく、本発明法により炭材の完
全燃焼がはかられ、かつ炭材の燃焼サイトと還元サイト
が分離できるため炭材使用量、酸素使用量の低減、吹錬
時間の短縮が可能となった。
As is clear from Table 2, the carbonaceous material can be completely burned by the method of the present invention, and the combustion site and the reduction site of the carbonaceous material can be separated. It became possible to shorten.

実施例2 10トン底吹き転炉を用い、第3表に示す原料配合条
件、および第4表に示す吹錬条件で半還元クロムペレッ
ト((%T.Cr)32.2、(%T.Fe)=21.6,Cr還元率62%,
Fe還元率87%)を溶融還元した結果、第5表に処理時
間,処理後溶銑,スラグ成分に示すごとく[%Cr]=1
5.8%の含クロム溶銑を70分にて溶製できた。
Example 2 Using a 10 ton bottom blowing converter, the semi-reduced chromium pellets ((% T.Cr) 32.2, (% T.Fe) under the raw material mixing conditions shown in Table 3 and the blowing conditions shown in Table 4 were used. = 21.6, Cr reduction rate 62%,
As a result of melt reduction of Fe reduction rate of 87%), [% Cr] = 1 as shown in Table 5 for treatment time, hot metal after treatment, and slag composition.
It was possible to melt 5.8% chromium-containing hot metal in 70 minutes.

発明の効果 以上説明したごとく、この発明方法によれば、クロム
鉱石等の溶融還元処理において、クロム酸化物、鉄酸化
物の迅速な還元進行を維持しながら、燃料(微粉炭、粉
コークス等)を酸素によりほぼ完全燃焼させ、かつ効率
よくスラグ浴・メタル浴を加熱することができるので、
大幅な燃料および酸素原単位の低減、並びに精錬時間の
短縮が可能となり、精錬コストの低減並びに生産性の向
上をはかることができる。
EFFECTS OF THE INVENTION As described above, according to the method of the present invention, in the smelting reduction treatment of chromium ore or the like, while maintaining the rapid reduction progress of chromium oxides and iron oxides, fuel (pulverized coal, powder coke, etc.) Since it can burn almost completely with oxygen and efficiently heat the slag bath / metal bath,
It is possible to significantly reduce the fuel and oxygen consumption rate and shorten the refining time, and it is possible to reduce refining costs and improve productivity.

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

第1図はこの発明方法を実施するための装置例を示す概
略図である。 1……転炉型反応容器、2……金属浴、3……スラグ
層、4……燃料および酸素吹込用横吹羽口、5……炭材
吹込用底吹羽口、6……CO燃焼用上吹ランス、7……CO
燃焼用横吹羽口。
FIG. 1 is a schematic view showing an example of an apparatus for carrying out the method of the present invention. 1 ... Converter-type reaction vessel, 2 ... Metal bath, 3 ... Slag layer, 4 ... Side blower for fuel and oxygen injection, 5 ... Bottom blower for carbon material injection, 6 ... CO combustion Ugebuki Lance, 7 ... CO
Side blowing tuyeres for combustion.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】クロム鉱石、クロム鉱石を前処理して製造
した未還元クロムペレット、半還元クロムペレット、ク
ロム焼結鉱等を石炭、コークス等の炭素源により溶融還
元してクロム含有量が39%以下のクロム含有溶鉄を製造
する方法において、スラグ浴内に炭素および水素を主成
分とする燃料と酸素を燃料がほぼ完全燃焼する比率で吹
込むことにより燃料を燃焼させてスラグ浴を加熱すると
ともに、金属浴中に石炭、コークス等の還元剤を吹込む
ことを特徴とするクロム含有溶鉄の製造方法。
1. A chromium ore, unreduced chromium pellets produced by pre-treating chromium ore, semi-reduced chromium pellets, chromium sintered ore, etc., are melt-reduced with a carbon source such as coal or coke to obtain a chromium content of 39. In the method for producing molten iron containing less than 50% chromium, the fuel containing carbon and hydrogen as main components and oxygen are blown into the slag bath at a rate at which the fuel is almost completely burned to burn the fuel and heat the slag bath. At the same time, a method for producing molten iron containing chromium, which comprises blowing a reducing agent such as coal or coke into a metal bath.
JP61259418A 1986-10-30 1986-10-30 Method for producing molten iron containing chromium Expired - Lifetime JPH0826378B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61259418A JPH0826378B2 (en) 1986-10-30 1986-10-30 Method for producing molten iron containing chromium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61259418A JPH0826378B2 (en) 1986-10-30 1986-10-30 Method for producing molten iron containing chromium

Publications (2)

Publication Number Publication Date
JPS63111108A JPS63111108A (en) 1988-05-16
JPH0826378B2 true JPH0826378B2 (en) 1996-03-13

Family

ID=17333828

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61259418A Expired - Lifetime JPH0826378B2 (en) 1986-10-30 1986-10-30 Method for producing molten iron containing chromium

Country Status (1)

Country Link
JP (1) JPH0826378B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4042176C2 (en) * 1990-12-29 1993-12-09 Tech Resources Pty Ltd Process for the reduction of metal oxides in the molten state
NL9500264A (en) * 1995-02-13 1996-09-02 Hoogovens Staal Bv Method for producing liquid pig iron.
NL9500600A (en) * 1995-03-29 1996-11-01 Hoogovens Staal Bv Device for producing liquid pig iron by direct reduction.
IT1284200B1 (en) * 1996-07-31 1998-05-08 Sviluppo Materiali Spa PROCEDURE FOR THE DIRECT PRODUCTION OF CAST IRON STARTING FROM FERRIFERO MATERIAL AND EQUIPMENT SUITABLE FOR THE EXECUTION OF

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54158320A (en) * 1978-06-03 1979-12-14 Nippon Steel Corp Refining method for high chromium steel
JPS59140349A (en) * 1983-01-27 1984-08-11 Nippon Steel Corp Method for increasing combustion rate of carbonaceous material under coexistence of large amount of slag
JPS624810A (en) * 1985-06-28 1987-01-10 Nippon Kokan Kk <Nkk> Refining furnace for iron making by melt reduction

Also Published As

Publication number Publication date
JPS63111108A (en) 1988-05-16

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