JPS61279609A - Apparatus for producing high-chromium alloy by melt reduction - Google Patents

Apparatus for producing high-chromium alloy by melt reduction

Info

Publication number
JPS61279609A
JPS61279609A JP12179585A JP12179585A JPS61279609A JP S61279609 A JPS61279609 A JP S61279609A JP 12179585 A JP12179585 A JP 12179585A JP 12179585 A JP12179585 A JP 12179585A JP S61279609 A JPS61279609 A JP S61279609A
Authority
JP
Japan
Prior art keywords
slag
oxygen
blowing
chromium
gas
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
Application number
JP12179585A
Other languages
Japanese (ja)
Other versions
JPH0421729B2 (en
Inventor
Takeyuki Hirata
平田 武行
Yujo Marukawa
雄浄 丸川
Masaharu Anezaki
姉崎 正治
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 JP12179585A priority Critical patent/JPS61279609A/en
Publication of JPS61279609A publication Critical patent/JPS61279609A/en
Publication of JPH0421729B2 publication Critical patent/JPH0421729B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/30Regulating or controlling the blowing
    • C21C5/35Blowing from above and through the bath
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/005Manufacture of stainless steel

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Steel In Its Molten State (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)

Abstract

PURPOSE:To produce a high-chromium alloy at a high yield with high efficiency by providing a top blowing lance and bottom blowing tuyeres in a refractory vessel contg. a metallic bath and providing side blowing tuyeres for slag to the vessel. CONSTITUTION:The metallic bath 2 is contained in a furnace 1 body and the slag 3 is formed above the bath 2. The top blowing lance 4 for blowing oxygen is sagged atop the slag 3 from an aperture 5 of the furnace body 1. On the other hand, the bottom blowing tuyeres 9, 9' for blowing a gas for stirring the metallic bath 2 are provided to the bottom of the furnace body 1. The side blowing tuyeres 6, 6' for blowing oxygen or the gas enrichedwith oxygen and an inert gas such as N2 or CO2 to the inside of the slag 3 are provided to the wall part of the body 1. The chromium reduction in the slag 3 is efficiently executed if the chromium raw material, carboneous material and fluxing agent are fed out of the banker 8 and the high-chromium alloy steel is produced by the melt reduction.

Description

【発明の詳細な説明】 11よp男月分! 本発明は酸素上吹き炉の如き精錬炉を用いて溶融還元に
より高クロム合金を製造する装置に関する。
[Detailed description of the invention] 11yo pmangetsubu! The present invention relates to an apparatus for producing high chromium alloys by smelting reduction using a refining furnace such as an oxygen top-blown furnace.

より詳細には本発明は、酸素上吹きランスを備える精錬
炉であって、主としてスラグ中でクロム還元を行うのに
適した、溶融還元によりステンレス鋼の如き高クロム合
金を製造する装置に関する。
More particularly, the present invention relates to a smelting furnace equipped with an oxygen top-blowing lance, which is suitable primarily for carrying out chromium reduction in slag, and for producing high chromium alloys, such as stainless steel, by smelting reduction.

従来の技術 従来、ステンレス鋼等の高クロム鋼は、クロム鉱石を電
気炉においてコークスにより還元して高炭素フェロクロ
ムを製造し、これを原料として溶製されてきた。すなわ
ち、この方式は、Cr%が高い鉱石の還元が進行するた
めには高温度が必要であるため、これを過剰量の炭材(
コークス)の存在下で電気炉で行い、得られたフェロク
ロムを鉄源とともに再度溶解、脱炭して高クロム鋼を製
造する2段階の方法である。
BACKGROUND ART Conventionally, high chromium steel such as stainless steel has been produced by reducing chromium ore with coke in an electric furnace to produce high carbon ferrochrome, and using this as a raw material. In other words, in this method, high temperatures are required for the reduction of ores with high Cr% to proceed, so they are treated with an excessive amount of carbonaceous material (
This is a two-step method in which high chromium steel is produced by melting the obtained ferrochrome together with an iron source and decarburizing it again in an electric furnace in the presence of coke.

しかしながら、“間接製造法”と称するこの方式には、
クロム鉱石からステンレス鋼までの一貫の流れとして見
た場合、次のような問題点がある。
However, this method called “indirect manufacturing method” has
When viewed as a consistent flow from chrome ore to stainless steel, there are the following problems.

(1)クロム酸化物の還元に要する多量のエネルギーと
して、高価な電力を用いている。
(1) Expensive electricity is used as the large amount of energy required to reduce chromium oxide.

(2)一般にフェロクロム製造工場と製鋼工場は離れて
いるため、高炭素フェロクロムは溶融物として製造され
ながら、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。
(2) Since ferrochrome manufacturing plants and steelmaking plants are generally located far apart, high-carbon ferrochrome is produced as a molten product, but it is solidified once and then remelted during the steelmaking process, resulting in large energy losses.

(3)多量のスラグが(Cr%)の高いフエムクロムと
接触した状態で精錬されるので、スラグ中の(Cr%)
を低くすることがむずかしく、クロム損失が大きい。
(3) Since a large amount of slag is smelted in contact with FEM chrome with high (Cr%), the (Cr%) in the slag
It is difficult to lower the chromium loss, and the loss of chromium is large.

従って、高クロム鋼の溶製のコスト低減のためにはこれ
らの問題を解決することが必要であり、次のような対策
が考えられた。すなわち、(1)クロム鉱石の還元エネ
ルギーとして、電力ではなく安価な一次エネルギーを使
用すること、(2)クロム鉱石からステンレス鋼までの
一貫工程としてエネルギー損失が最小となるようにする
こと、 (3)スラグを最小量とし、Cr回収率の高い反応また
は反応環境とすること、 が必要である。
Therefore, in order to reduce the cost of melting high chromium steel, it is necessary to solve these problems, and the following measures have been considered. In other words, (1) use cheap primary energy instead of electricity as energy for reducing chromium ore, (2) minimize energy loss in the integrated process from chromium ore to stainless steel, (3) ) It is necessary to minimize the amount of slag and create a reaction or reaction environment with a high Cr recovery rate.

このような技術思想のもとに、例えば特開昭54−15
8320号に底吹き転炉によりクロム鉱石からクロム鋼
を製造する方法が提案されている。         
  1しかしながら、溶銑にクロム鉱石を直接投入し 
      □た場合、クロム鉱石の主成分たるMgO
”CrzOaな       )どの難溶性クロマイト
を還元することは容易でない。効率よく還元するために
は、SiO・やCaO等       :を加え、Mg
O・Cr2O*のスラグ中への溶解を促進      
 iする必要がある(公知文献 興梠ら、鉄と鋼亘  
     1(1984)  S、114)。
Based on this technical idea, for example, Japanese Patent Application Laid-Open No. 54-15
No. 8320 proposes a method for producing chromium steel from chromium ore using a bottom-blown converter.
1 However, if chromium ore is directly added to hot metal,
□If MgO is the main component of chromium ore,
It is not easy to reduce poorly soluble chromite such as CrzOa.In order to reduce it efficiently, it is necessary to add SiO, CaO, etc., and
Promotes dissolution of O・Cr2O* into slag
It is necessary to
1 (1984) S, 114).

このような問題を解決するために、特開昭60−981
5号公報には、溶湯温度を1650℃以下に保つととも
に、炉底より吹込まれるガス量を制御し、スラグ組成お
よび遊離炭材量を制限して溶融還元する方法が開示され
ている。しかしながら、この方法ではクロムを還元する
ためにスラグの強攪拌を行う必要があるが、この攪拌力
をメタルの攪拌を介してスラグに伝える点で、精錬操作
上大きな難点がある。即ち、メタル攪拌ガス量が極めて
多いため、非0□系ガスではメタル温度の低下を招きや
すい。温度維持のため0□を含ませると、メタル中のク
ロムの酸化を招くジレンマがある。また、第2期終了後
のスラグとメタルの分離の際、吹込みガス量を減少しに
くいため、スラグ中懸濁粒鉄としてのメタルロスの増加
を招く欠点がある。
In order to solve such problems, Japanese Patent Application Laid-Open No. 60-981
Publication No. 5 discloses a method of melting and reducing the molten metal by keeping the temperature of the molten metal at 1650° C. or lower, controlling the amount of gas blown in from the bottom of the furnace, and limiting the slag composition and the amount of free carbon materials. However, this method requires strong stirring of the slag in order to reduce chromium, but there is a major difficulty in refining operations in that this stirring force is transmitted to the slag through stirring of the metal. That is, since the amount of metal stirring gas is extremely large, non-0□ type gas tends to cause a drop in metal temperature. If 0□ is included in order to maintain the temperature, there is a dilemma of oxidation of chromium in the metal. Furthermore, when separating the slag and metal after the second stage, it is difficult to reduce the amount of blown gas, resulting in an increase in metal loss as suspended particulate iron in the slag.

発明の解決しようとする問題点 本発明の目的は、上記した従来技術の問題を解決するこ
とにあり、より詳細には炉内耐火物の過大な損耗を招く
ことなく、クロム還元を高収率で実現しうる溶融還元に
よる高クロム合金の製造装       1・置を提供
することにある。
Problems to be Solved by the Invention The purpose of the present invention is to solve the problems of the prior art described above, and more specifically, to reduce chromium in a high yield without causing excessive wear and tear on the refractories in the furnace. An object of the present invention is to provide an apparatus for producing high chromium alloys by smelting reduction that can be realized in 1.

問題点を解決する手段 本発明者等は上記した本発明の目的を達成する    
  まため種々の実験、検討を重ねた結果、次の知見を
      1得、本発明を完成したものである。  
           □1゜ ■ 特開昭54−158320号および特開昭60−9
815号公報に開示の方法では上底吹転炉を使用して 
     1クロム還元を行っているが、本来還元性雰
囲気であるべき金属浴中に酸素を吹込むと還元されたク
ロムを再酸化してクロム還元速度を遅くする。また、金
属浴中に微粉炭を底吹きするには専用の吹込み設備が必
要であり、ランニングコストも高くなる。
Means for Solving the Problems The present inventors achieve the above-mentioned objects of the present invention.
As a result of various experiments and studies, we have obtained the following knowledge and completed the present invention.
□1゜■ JP-A-54-158320 and JP-A-60-9
The method disclosed in Publication No. 815 uses a top-bottom blowing converter.
1 chromium reduction is performed, but when oxygen is blown into the metal bath, which should originally be a reducing atmosphere, the reduced chromium is re-oxidized and the chromium reduction rate is slowed down. In addition, special blowing equipment is required to bottom blow pulverized coal into a metal bath, which increases running costs.

■ 一方、溶融還元ではスラグ中でクロム還元を行ない
、金属浴は還元されて降下するクロムを回収する媒体と
して扱い、スラグおよび金属浴を別々に管理することが
反応効率、熱管理および炉内耐火物の原単位向上の点か
ら極めて好ましいことが解った。
■ On the other hand, in smelting reduction, chromium is reduced in slag, and the metal bath is treated as a medium to recover the chromium that falls due to reduction. Separate management of the slag and metal bath improves reaction efficiency, heat management, and fire resistance in the furnace. It was found that this is extremely preferable from the point of view of improving the basic unit of production.

■ すなわち、クロムの還元反応効率および回収率を向
上させるためにスラグの化学組成、温度および還元雰囲
気を最適に調整し、一方、金属浴は温度を均一に保持す
る程度の攪拌を行えば十分である。
■ In other words, it is sufficient to optimally adjust the chemical composition, temperature, and reducing atmosphere of the slag in order to improve the efficiency of the chromium reduction reaction and the recovery rate, while stirring the metal bath to the extent that it maintains a uniform temperature is sufficient. be.

■ このような技術思想のもとにクロム鉱石投入口等の
熱源を多量に必要とする期間は酸素を上吹きすることは
もらろん、スラグ内にも酸素または酸素富化ガスを吹込
み、加熱およびスラグ攪拌の強化を図る。一方、炉底か
らは攪拌ガスを吹込み、金属浴の温度を均一とし、金属
浴の加熱はスラグとの接触による伝導加熱のみとする。
■ Based on this technical idea, during periods when a large amount of heat source is required, such as at the chromium ore inlet, oxygen is not top-blown, but oxygen or oxygen-enriched gas is also blown into the slag. Heating and slag stirring will be strengthened. On the other hand, stirring gas is blown from the bottom of the furnace to make the temperature of the metal bath uniform, and the metal bath is heated only by conduction heating through contact with the slag.

また、クロム鉱石の投入完了後等、熱源をあまり必要と
しない期間は、上吹酸素量を減少させ、発熱量と吸熱量
とのバランスをとるほかスラグ内へ吹込むガスの酸素濃
度を減らす。
In addition, during periods when a heat source is not required, such as after the completion of charging chromium ore, the amount of top-blown oxygen is reduced to maintain a balance between calorific value and heat absorption, and to reduce the oxygen concentration of the gas blown into the slag.

熱バランスが十分とれればスラグ内の還元雰囲気を一層
強化する目的でN2、CO2、COなどの不活性ガスを
用いる方がさらに望ましい。この際も、当然メタル内の
攪拌に酸素は用いず、スラグからの伝導加熱に徹する。
If a sufficient heat balance is achieved, it is more desirable to use an inert gas such as N2, CO2, or CO in order to further strengthen the reducing atmosphere within the slag. At this time, of course, oxygen is not used for stirring inside the metal, and heating is carried out through conduction from the slag.

このようなりロム還元方法を実現するには特別な装置を
必要とし、特にスラグのみを効率よく加熱する手段を設
けることが必要となる。
In order to realize such a ROM reduction method, a special device is required, and in particular, it is necessary to provide a means for efficiently heating only the slag.

以上の如き知見に基づき本発明は完成されたものであっ
て、本発明に従い、内部に金属浴を収容する耐火性容器
と、該耐火性容器の金属浴面下に設けられて該金属浴内
に攪拌ガスを吹込む羽口と、該耐火性容器の上方開口部
から酸素を吹込む上吹きランスと、該金属浴上に形成さ
れるスラグの表面下であって且つ該金属浴面の上方に位
置する該耐火性容器の壁部に設けられ、該スラグ内に酸
素または酸素富化ガスおよびN2、CO2、COなどの
不活性ガスを吹込む羽口とを備えることを特徴とする溶
融還元による高クロム合金製造装置が提供される。
The present invention has been completed based on the above knowledge, and according to the present invention, there is provided a fireproof container which houses a metal bath therein, and a fireproof container which is provided under the surface of the metal bath of the fireproof container and which is provided inside the metal bath. a tuyere for blowing stirring gas into the refractory container; a top-blowing lance for blowing oxygen from the upper opening of the refractory container; A smelting reduction characterized by comprising a tuyere provided on the wall of the refractory container located at the slag for blowing oxygen or oxygen-enriched gas and an inert gas such as N2, CO2, CO into the slag. A high chromium alloy manufacturing apparatus is provided.

本発明の好ましい態様に従うと、上記したスラグ内に酸
素または酸素富化ガスおよびN2、CO2、COなどの
不活性ガスを吹込む羽口(以下、“横吹き羽口”という
)は、耐火性容器の垂直軸心とはずれて方向ずけられて
いる。また、複数の横吹き羽口を備えているときには、
耐火性容器の周囲にほぼ等間隔に配置され、且つスラグ
を回転状に攪拌するように垂直軸心よりはゾ同−角度だ
けずれて方向づけられているのが好ましい。
According to a preferred embodiment of the present invention, the tuyeres (hereinafter referred to as "side-blown tuyeres") for blowing oxygen or oxygen-enriched gas and inert gases such as N2, CO2, CO, etc. into the slag are refractory. Oriented off the vertical axis of the container. Also, when equipped with multiple side-blown tuyeres,
Preferably, they are spaced approximately equally spaced around the refractory vessel and oriented at an angle offset from the vertical axis to provide rotational agitation of the slag.

さらに、本発明の好ましい態様に従うと、横吹き羽口は
二重管から構成され、内管は酸素源に連結されており、
一方、外管は冷却用ガス源に連結されている。
Furthermore, according to a preferred embodiment of the invention, the side-blown tuyere is constructed from a double pipe, the inner pipe being connected to an oxygen source,
Meanwhile, the outer tube is connected to a cooling gas source.

冷却用ガスとしては窒素、アルゴン等の不活性ガスの他
、Co、CO2であってもよい。
The cooling gas may be an inert gas such as nitrogen or argon, as well as Co or CO2.

詐月 本発明の高クロム合金製造装置では、スラグは上吹きラ
ンスおよび横吹きランスによって酸素を吹込まれ、一方
、金属浴には底吹き羽口から攪拌ガスのみが吹込まれる
。従って、スラグ中の炭材は酸素によって燃焼し、スラ
グを加熱するとともにスラグ中のクロム原料を還元し、
一方、金属浴はスラグとの接触によってのみ加熱される
とともに攪拌によって均熱化される。
In the high chromium alloy manufacturing apparatus of the present invention, the slag is blown with oxygen by the top blowing lance and the side blowing lance, while only the stirring gas is blown into the metal bath from the bottom blowing tuyere. Therefore, the carbonaceous material in the slag is burned by oxygen, heating the slag and reducing the chromium raw material in the slag.
On the other hand, the metal bath is heated only by contact with the slag and is uniformly heated by stirring.

このようにして、スラグ中でのクロム還元が最適となる
ようにスラグ温度および還元雰囲気を金属浴とは別個に
調節でき、一方、金属浴中に酸素を吹込まないので金属
浴中のクロムの再酸化を防止し、高効率および高収率の
クロム還元を達成するとともに、耐火物の原単位を低減
することかできる。
In this way, the slag temperature and reducing atmosphere can be adjusted separately from the metal bath so that the chromium reduction in the slag is optimized, while the chromium reduction in the metal bath is not blown into the metal bath. It is possible to prevent reoxidation, achieve high efficiency and high yield chromium reduction, and reduce the unit consumption of refractories.

実施例 以下、添付の図面を参照して実施例により本発明を説明
するが、これらの実施例は本発明の車なる例示であって
、本発明の技術的範囲を何隻制限するものではない。
EXAMPLES Hereinafter, the present invention will be explained by examples with reference to the accompanying drawings, but these examples are merely illustrative of the vehicles of the present invention, and do not limit the technical scope of the present invention. .

第1図は本発明に従う高クロム合金製造装置の1実施例
の断面概略図であり、第2図は第1図に示した装置内の
スラグと吹込み酸素とが接触する領域を示す模式図であ
る。
FIG. 1 is a schematic cross-sectional view of one embodiment of the high chromium alloy manufacturing apparatus according to the present invention, and FIG. 2 is a schematic diagram showing the area where slag and blown oxygen come into contact in the apparatus shown in FIG. It is.

第1図に示す装置は上底吹転炉を改造した精錬    
   ;炉であるが、本発明の装置は転炉型でなくとも
、       1゜)パ 例えば電気炉を改造したものであってもよい。    
    1・!・ 第1図において、炉体1は例えばマグネシア−・クロメ
ートレンガで内張すされたものであって、この炉体1の
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。金属浴2の上方にはスラグ3が形成され、スラグ
3の上面に酸素を吹き込むための上吹きランス4が炉体
1の開口部5の上方から垂下して設けられ、一方、スラ
グ3内に酸素または酸素富化ガスおよびN2、CO□、
c。
The equipment shown in Figure 1 is a smelter that is a modified upper-bottom blowing converter.
Although it is a furnace, the apparatus of the present invention does not have to be a converter type, and may be a modified electric furnace, for example.
1.! - In FIG. 1, a furnace body 1 is lined with, for example, magnesia-chromate bricks, and a metal bath 2, for example hot metal or molten steel, is accommodated inside the furnace body 1. A slag 3 is formed above the metal bath 2 , and a top blowing lance 4 for blowing oxygen into the top surface of the slag 3 is provided hanging down from above the opening 5 of the furnace body 1 . Oxygen or oxygen-enriched gas and N2, CO□,
c.

などの不活性ガスを吹込むための横吹き羽口6.6°が
炉体1の炉壁部に設けられている。 さらに、炉体1の
開口部5には排ガス回収フード7が着脱可能に付設され
、またクロム鉱石、還元ペレット等のクロム原料、コー
クス等の炭材及び媒溶剤を炉内に添加するバンカー8が
設けられている。
A horizontal blowing tuyere of 6.6° for blowing inert gas such as the like is provided on the furnace wall of the furnace body 1. Further, an exhaust gas recovery hood 7 is removably attached to the opening 5 of the furnace body 1, and a bunker 8 is provided for adding chromium raw materials such as chromium ore and reduced pellets, carbon materials such as coke, and solvents into the furnace. It is provided.

一方、炉体1の炉底部には金属浴2を攪拌するためにガ
スを吹込む羽口9.9°が設けられている。
On the other hand, a tuyere 9.9° is provided at the bottom of the furnace body 1 to blow gas into the metal bath 2 in order to stir it.

本発明の装置を用いて溶融還元により高クロム合金鋼を
製造するには、バンカー8よりクロム原料、炭材および
媒溶材を切り出し、溶鋼からなる金属浴2上に投入し、
上吹きランス4より酸素を吹込み横吹き羽口6.6゛か
ら酸素または酸素富化ガスを吹込んでスラグ3を形成す
る。
To produce high chromium alloy steel by smelting reduction using the apparatus of the present invention, chromium raw materials, carbonaceous materials, and solvent materials are cut out from the bunker 8 and placed onto the metal bath 2 made of molten steel.
The slag 3 is formed by blowing oxygen through the top blowing lance 4 and blowing oxygen or oxygen-enriched gas through the side blowing tuyere 6.6''.

上吹きランス4及び横吹き羽口6.6”から吹込まれる
酸素と接触するスラグの部分を第2図に示すが、図示の
如く、上吹きランス4から吹込まれる酸素とスラグとの
接触部分a、と、横吹き羽口6.6”から吹込まれる酸
素とスラグとの接触部分a2とはスラグ3の水平断面の
可成りの部分を占めている。また横吹き羽口6.6°の
吹込み方向は炉体1の水平断面の半径方向とずれて設定
されており、このためスラグが効果的に攪拌され、一方
上吹きランス4は高さ位置及び水平位置を変えることに
より酸素のスラグとの接触部分alの面積が大となるよ
うに調節するのが好ましい。
Figure 2 shows the portion of the slag that comes into contact with oxygen blown from the top blow lance 4 and the side blow tuyere 6.6''. The portion a and the contact portion a2 between the slag and the oxygen blown from the side blowing tuyere 6.6'' occupy a considerable portion of the horizontal cross section of the slag 3. In addition, the blowing direction of the horizontal blowing tuyere 6.6° is set to be offset from the radial direction of the horizontal cross section of the furnace body 1, so that the slag is effectively stirred, while the top blowing lance 4 is placed at a height position. It is preferable to adjust the area of the contact portion al of oxygen with the slag to be large by changing the horizontal position.

以上の如く、バンカー8から炭材のみを投入し且つスラ
グ3内に酸素を吹込み、炭材を酸化してスラグを加熱す
るとともに、スラグ中のクロム還       1元を
行う。一方、炉底羽口9.9°から攪拌ガスが吹込まれ
、金属浴2は攪拌されると同時に、ス       1
ラグ3との接触により伝導加熱される。−従って、  
     )金属浴2は酸素と接触することなく・還元
性雲間      I気に保持され、スラグ中で還元さ
れたクロムを受け、また上記の如くスラグにより加熱さ
れるので流動性を保持できる。
As described above, only the carbonaceous material is introduced from the bunker 8 and oxygen is blown into the slag 3 to oxidize the carbonaceous material and heat the slag, and at the same time, chromium reduction in the slag is carried out. On the other hand, stirring gas is blown into the furnace bottom tuyere 9.9°, and the metal bath 2 is stirred at the same time.
Contact with the lug 3 causes conductive heating. -Therefore,
) The metal bath 2 is held in a reducing cloud without contacting oxygen, receives chromium reduced in the slag, and is heated by the slag as described above, so that fluidity can be maintained.

こうしたスラグ形成が終了すると、バンカー8からのク
ロム原料、媒溶剤の投入を停止し、炭剤のみを投入し、
横吹き羽口6.6゛からN2、C02、COなどの不活
性ガスを、底吹き羽口9.9°からは窒素等の攪拌ガス
を吹込む。
When this slag formation is completed, the injection of the chromium raw material and solvent from the bunker 8 is stopped, and only the carbonaceous agent is introduced.
Inert gas such as N2, CO2, CO, etc. is blown from the side blowing tuyere at 6.6°, and stirring gas such as nitrogen is blown from the bottom blowing tuyere at 9.9°.

第3図は二重管からなる横吹き羽口の断面概略図である
。この横吹き羽口は内管11および外管12からなり、
内管11は酸素源(図示せず)に連結されて、スラグ3
内に酸素を吹込むように構成され、外管12は冷却ガス
源(図示せず)に連結され、内管11を冷却しながら、
スラグ内にガスを吹込む。
FIG. 3 is a schematic cross-sectional view of a horizontal blowing tuyere made of double pipes. This side-blown tuyere consists of an inner pipe 11 and an outer pipe 12,
Inner tube 11 is connected to an oxygen source (not shown) to supply slug 3
The outer tube 12 is connected to a cooling gas source (not shown) to cool the inner tube 11 while cooling the inner tube 11.
Inject gas into the slag.

この冷却ガスは内管11を冷却した後、スラグ内に吹込
まれてスラグを攪拌する。
After cooling the inner tube 11, this cooling gas is blown into the slag to agitate the slag.

名…p皇】 以上詳述の如く、本発明に伴う溶融還元による高クロム
合金の製造装置は、従来の装置と異なりスラグ内にあみ
酸素または酸素富化ガスおよびN2、CO□、GOなど
の不活性ガスを吹込む専用の羽       ]口を備
えており、スラグ内でクロム還元を効率よ      
 [〈実施するのに極めて好適である。       
      社また、金属浴は単に攪拌されるのみで酸
素を吹      1込まれないので金属浴内でのクロ
ムの再酸化も生      1゜ぜず、攪拌された金属
浴は均一温度に保たれて、       iし その溶融状態を保持する。             
    [従って、溶融還元による高クロム合金の製造
に      F際して、り・ム還元をスラグ内で行う
ようにスラ      −′グを金属浴とは別個に温度
および還元雰囲気の調      [1・ 整を行うことができ、高効率且つ高収率の高クロ   
   [lム合金の製造を行うのに最適である。   
         l・11′
As described in detail above, the apparatus for producing high chromium alloy by smelting reduction according to the present invention differs from conventional apparatus in that the slag contains oxygen or oxygen-enriched gas and N2, CO□, GO, etc. Equipped with a dedicated blade for blowing inert gas, it efficiently reduces chromium in the slag.
[<Extremely suitable for implementation.]
Furthermore, since the metal bath is simply stirred and no oxygen is blown into it, re-oxidation of chromium does not occur within the metal bath, and the stirred metal bath is kept at a uniform temperature. Maintains the molten state of perilla.
[Therefore, when manufacturing high chromium alloys by smelting reduction, the temperature and reducing atmosphere of the slag must be adjusted separately from the metal bath so that the rim reduction takes place within the slag [1. can be carried out with high efficiency and high yield.
[Ideal for manufacturing aluminum alloys.]
l・11'

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

第1図1よ本発明1.従う高、。4合金製造装置。  
    111実施例の断面概略図であり、     
          盲。 lI′ 第2図は第1図に示した装置内のスラグと吹込    
  にみ酸素とが接触する領域を示す模式図であり、 
       、)、、第3図は二重管からなる横吹き
羽口の断面概略      [:九 i′:′ 図1あ6・                    
    Ill b: (主な参照番号) 1・・・炉体、  2・・・金属浴、 3・・・スラグ、  4・・・上吹きランス、6.6°
 ・・・横吹き羽口、 7・・・排ガス回収フード、 8・・・バンカー、 9.9° ・・・底吹き羽口、
Figure 1 1 This invention 1. High, follow. 4 alloy manufacturing equipment.
111 is a schematic cross-sectional view of Example 111,
Blind. lI' Figure 2 shows the slag and blowing in the equipment shown in Figure 1.
It is a schematic diagram showing a region in contact with oxygen.
, ), , Figure 3 is a schematic cross-sectional view of a horizontal blowing tuyere consisting of double pipes [:9i':' Figure 1A6.
Ill b: (Main reference numbers) 1...furnace body, 2...metal bath, 3...slag, 4...top blowing lance, 6.6°
...Side blowing tuyere, 7...Exhaust gas recovery hood, 8...Bunker, 9.9°...Bottom blowing tuyere,

Claims (3)

【特許請求の範囲】[Claims] (1)内部に金属浴を収容する耐火性容器と、該耐火性
容器のメタル浴面下に設けられて該金属浴内に攪拌ガス
を吹込む羽口と、該耐火性容器の上方開口部から酸素を
吹込む上吹きランスと、該金属浴上に形成されるスラグ
の表面下であって且つ該金属浴面の上方に位置する該耐
火性容器の壁部に設けられ、該スラグ内に酸素または酸
素富化ガスおよびN_2、CO_2、COなどの不活性
ガスを吹込む羽口とを備えることを特徴とする溶融還元
による高クロム合金製造装置。
(1) A fireproof container that houses a metal bath inside, a tuyere that is provided below the metal bath surface of the fireproof container to blow stirring gas into the metal bath, and an upper opening of the fireproof container. A top-blowing lance is provided on the wall of the refractory container located below the surface of the slag formed on the metal bath and above the metal bath surface, and is provided in the wall of the refractory container to blow oxygen into the slag. An apparatus for producing a high chromium alloy by smelting reduction, characterized by comprising a tuyere for blowing oxygen or oxygen-enriched gas and an inert gas such as N_2, CO_2, CO, etc.
(2)上記したスラグ内に酸素または酸素富化ガスおよ
びN_2、CO_2、COなどの不活性ガスを吹込む羽
口が、上記耐火性容器の垂直軸心とずれて方向づけられ
ていることを特徴とする特許請求範囲第1項記載の溶融
還元による高クロム合金製造装置。
(2) The tuyere for blowing oxygen or oxygen-enriched gas and inert gas such as N_2, CO_2, CO into the slag is oriented offset from the vertical axis of the refractory container. An apparatus for producing a high chromium alloy by melt reduction according to claim 1.
(3)上記したスラグ内に酸素または酸素富化ガスおよ
びN_2、CO_2、COなどの不活性ガスを吹込む羽
口が、二重管から構成され、内管から酸素または酸素富
化ガスが、外管から冷却用ガスが吹込まれることを特徴
とする特許請求の範囲第1項または第2項のいずれかに
記載の溶融還元による高クロム合金製造装置。
(3) The tuyeres for blowing oxygen or oxygen-enriched gas and inert gases such as N_2, CO_2, and CO into the slag described above are composed of double pipes, and oxygen or oxygen-enriched gas is injected from the inner pipe. 3. The apparatus for producing high chromium alloy by melt reduction according to claim 1 or 2, wherein cooling gas is blown into the outer tube.
JP12179585A 1985-06-05 1985-06-05 Apparatus for producing high-chromium alloy by melt reduction Granted JPS61279609A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12179585A JPS61279609A (en) 1985-06-05 1985-06-05 Apparatus for producing high-chromium alloy by melt reduction

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12179585A JPS61279609A (en) 1985-06-05 1985-06-05 Apparatus for producing high-chromium alloy by melt reduction

Publications (2)

Publication Number Publication Date
JPS61279609A true JPS61279609A (en) 1986-12-10
JPH0421729B2 JPH0421729B2 (en) 1992-04-13

Family

ID=14820098

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12179585A Granted JPS61279609A (en) 1985-06-05 1985-06-05 Apparatus for producing high-chromium alloy by melt reduction

Country Status (1)

Country Link
JP (1) JPS61279609A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0436718A1 (en) * 1987-09-10 1991-07-17 Nkk Corporation Method of charging ore in melt-reduction

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0436718A1 (en) * 1987-09-10 1991-07-17 Nkk Corporation Method of charging ore in melt-reduction

Also Published As

Publication number Publication date
JPH0421729B2 (en) 1992-04-13

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