JPS6260813A - Continuous refining method - Google Patents
Continuous refining methodInfo
- Publication number
- JPS6260813A JPS6260813A JP19935885A JP19935885A JPS6260813A JP S6260813 A JPS6260813 A JP S6260813A JP 19935885 A JP19935885 A JP 19935885A JP 19935885 A JP19935885 A JP 19935885A JP S6260813 A JPS6260813 A JP S6260813A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- oxygen
- decarburization
- lance
- blown
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/285—Plants therefor
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/56—Manufacture of steel by other methods
- C21C5/567—Manufacture of steel by other methods operating in a continuous way
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Botany (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は、金属あるいは合金、とくにステンレス鋼のよ
うな高クロム合金鋼をカーボン含有量を極く低くシ、安
価でかつ収率よく製造するための連続精錬方法に関する
ものである。[Detailed Description of the Invention] [Technical Field of the Invention] The present invention is directed to producing metals or alloys, particularly high chromium alloy steels such as stainless steel, with extremely low carbon content, at low cost, and with high yield. The present invention relates to a continuous refining method.
製鉄工業において使用する製鉄法としては、従来より各
種のものが提案されている。Various types of iron manufacturing methods have been proposed for use in the iron manufacturing industry.
具体的には例えば、ドレド(Dored)法、エルレド
(ELRED)法、インレット(INRED)法、コイ
ン(COIN)法、KR法、川崎製鉄法、住人金属法な
どと称されているものがある。Specifically, there are methods known as the Dored method, the ELRED method, the INRED method, the COIN method, the KR method, the Kawasaki Steel method, and the Sumitomo Metal method.
これらの従来のもののほか、省資源対策の一貫として、
この種の製鉄技術においてもナショナルプロジェクト的
な協同研究開発が開始され、その成果が徐々に現れはじ
めている。In addition to these conventional measures, as part of resource saving measures,
Collaborative research and development as a national project has begun on this type of steelmaking technology, and the results are gradually beginning to appear.
これらの方法のいずれもが、それぞれ特徴を有するもの
であり、そこに付随している精錬方法にも、当然のこと
ながら、それぞれにおいて特徴をもたせた各種の形態の
ものがある。All of these methods have their own characteristics, and the refining methods that accompany them naturally come in various forms, each with its own characteristics.
例文ば、
fil Ts電気炉鉱石を還元して得たフェロクロム
溶湯を凝固させて、合金鉄としてステンレス製造時にこ
れをクロム源として使用する方法や(2) クロム鉱
石に炭材、フラックスを添加し、酸素を供給して得たフ
ェロクロム溶湯を凝固させ、合金鉄としてステンレス製
造時にこれをクロム源として使用する方法や
(3) 電気炉で鉱石を還元して得たフェロクロム溶
湯をそのまま別途のステンレス製造プロセスで使用する
方法、あるいは
(4) 溶銑にクロム鉱石を添加し酸素を供給しなが
ら、炭材、フラックスを加えてクロム相溶湯を製造し、
その後脱炭およびクロムI成分調整を行う方法、
などがある。For example, ferrochrome molten metal obtained by reducing fil Ts electric furnace ore is solidified and used as a chromium source when producing stainless steel as a ferroalloy; (2) adding carbon and flux to chromium ore; There is a method in which the ferrochrome molten metal obtained by supplying oxygen is solidified and used as a ferroalloy as a chromium source when manufacturing stainless steel, and (3) a separate stainless steel manufacturing process in which the ferrochrome molten metal obtained by reducing ore in an electric furnace is directly used. or (4) add chromium ore to hot metal and while supplying oxygen, add carbonaceous material and flux to produce chromium-compatible metal,
There are methods such as decarburization and adjustment of chromium I content after that.
これらの精練法のうら、従来高クロム合金鋼、例えばス
テンレスのような合金鋼は、クロム鉱石を電気炉で加熱
、溶融、還元して製造されたフェロクロム合金を合金鉄
製品とし、別の場所、別の機会にスクラップ、溶銑等の
他の鉄源と共に電気炉、転炉で溶解、精練するプロセス
を経て製造されるのが一般的であった。In addition to these smelting methods, conventional high chromium alloy steels, such as stainless steel, are produced by heating, melting, and reducing chromium ore in an electric furnace. Generally, it was manufactured through a process of melting and refining it in an electric furnace or converter furnace along with other iron sources such as scrap and hot metal.
ところが、これらの技術にあっては、次のような問題点
を潜在的に有し、あるいは顕在させているものであった
。However, these techniques have latent or actual problems as described below.
先ず、電気炉を用いるときは、膨大な量の電力を必要と
するため、経済性の観点からすればかならずしも有利な
ものではなく、より経済的な方法の確立がのぞまれてい
た。゛
また、クロム源を合金鉄として凝固させてから後で他の
鉄源と溶解しクロム合金鋼を製造したのでは、エネルギ
ー的にみれば不利である。First, since the use of an electric furnace requires a huge amount of electricity, it is not necessarily advantageous from an economical point of view, and there has been a desire to establish a more economical method. Furthermore, it is disadvantageous from an energy standpoint to produce chromium alloy steel by solidifying a chromium source as a ferroalloy and then melting it with other iron sources.
さらにまた、従来電気炉または転炉におけるステンレス
粗溶湯あるいは高炭素フェロクロム粗溶湯の溶解、精練
工程、例又はクロム鉱石の還元によるフェロクロムの溶
製、フェロクロム合金鉄と他の鉄源の溶解、含クロム粗
溶湯の脱炭等の処理や行うにあたっては、−穀的にはバ
ッチ方式を採用しており生産量に応じた大容量の炉を必
要とすることである。Furthermore, melting of crude stainless steel melt or crude high carbon ferrochrome melt in a conventional electric furnace or converter, smelting process, e.g., melting of ferrochrome by reduction of chromium ore, melting of ferrochrome alloy iron and other iron sources, chromium-containing In processing and carrying out decarburization of crude molten metal, a batch method is adopted for grains, and a large-capacity furnace is required according to the production volume.
例えば、前述のナショナルプロジェクトの場合、3t程
度のクロムを約60%含む溶湯を15を程度規模の上底
吹き型の転炉において処理するという様な処理方法を採
用している。For example, in the case of the above-mentioned national project, a processing method is adopted in which about 3 tons of molten metal containing about 60% chromium is processed in a top-bottom blowing converter of about 15 mm in size.
これは、炭材を供給しながら溶湯を作っているが、鉱石
には脈石が混入していることから、例えば1tのクロム
を約60%含む溶湯を製造するのに約1tのスラグが副
生する。This is because molten metal is made while supplying carbonaceous materials, but because gangue is mixed in with the ore, for example, to produce 1 ton of molten metal containing about 60% chromium, about 1 ton of slag is added. live.
ところが、このものの密度は、およそ1/3であるため
にその容積は膨大なものとなり、従ってこれが大容量の
炉を必要とする原因であった。However, since the density of this material is about 1/3, its volume becomes enormous, and this is the reason why a large-capacity furnace is required.
本発明は、このような状況の中にあって、電力を使用せ
ず、エネルギー源として安価な炭材を用いて直接鉱石を
還元してクロム源を製造することができれば有利であろ
うとの1iff点から粗溶湯を精練ずろ技術について種
々検討を加えた結果、溶融還元炉と脱炭炉とを連結させ
、溶融還元炉では、ランスから酸素ガスを供給し、炉下
部羽口から酸素および窒素またはアルゴンガスのうちの
1つ以上の賀すを吹き込む一方、鉱石、炭材、石灰等の
フラックスをこれらガスと共にまたは単独に供給して還
元反応を行わせ、ここから送り出される溶湯に予備処理
溶銑を添加しつつ、連続的にこれを脱炭炉に導き、ここ
でランスから酸素を、またアルゴン、窒素および酸素を
炉下部羽口から吹き込んで、脱炭反応と成分調整とを行
なわせることからなる連続精錬方法に到達したのである
。The present invention is based on the idea that it would be advantageous to directly reduce ore to produce a chromium source using inexpensive carbonaceous materials as an energy source without using electricity. As a result of various studies on scouring technology for crude molten metal, we connected a smelting reduction furnace and a decarburization furnace, and in the smelting reduction furnace, oxygen gas was supplied from a lance, and oxygen and nitrogen or While one or more gases of argon gas are injected, a flux of ore, carbonaceous material, lime, etc. is supplied together with these gases or alone to cause a reduction reaction, and pre-treated hot metal is added to the molten metal sent from there. This is a continuous process in which the decarburization reaction and component adjustment are carried out by continuously leading the carbon to the decarburization furnace, where oxygen is blown from the lance, and argon, nitrogen, and oxygen are blown from the tuyere at the bottom of the furnace. The refining method has been achieved.
以下、図面を用いて本発明の構成をより詳細に説明する
。Hereinafter, the configuration of the present invention will be explained in more detail using the drawings.
図面は、本発明を実施する際に使用する装置の一例を示
したもので、先ず、溶融還元炉1の炉上部から例えば、
クロム鉱石、炭材を原料供給ランス2を通して供給する
とともに酸素の吹き込みを別途のランス3を通じて行い
、一方、これとは別に酸素およびアルゴンを炉の下側の
羽口4から吹き込んで、溶融還元反応を行わせ高炭素フ
エロクロム溶湯を製造するのである。The drawing shows an example of the apparatus used when carrying out the present invention. First, from the upper part of the melting reduction furnace 1, for example,
Chromium ore and carbonaceous materials are supplied through the raw material supply lance 2, and oxygen is blown in through a separate lance 3.Otherwise, oxygen and argon are blown in through the tuyere 4 at the bottom of the furnace to initiate the melting and reduction reaction. This process produces high carbon ferrochrome molten metal.
なお、この溶融還元炉1の上部には、別途にスクラップ
、クロム鉱石、炭材、フラックスを投入するための投入
口5を有すると共に、脱ガス用排気口6を有しているも
のである。The upper part of the melting reduction furnace 1 has an input port 5 for separately inputting scrap, chromium ore, carbonaceous material, and flux, and also has an exhaust port 6 for degassing.
この溶融還元炉1では、還元反応が連続的に進行し、反
応が終了したものから順次に高炭素7エロクロム溶湯と
して出湯する。In this melting reduction furnace 1, the reduction reaction proceeds continuously, and the high-carbon 7-erochrome molten metal is tapped out one after another after the reaction has been completed.
との溶湯は次いで、脱炭炉7に導かれるが、導入に先立
ち予備処理溶銑を添加しつつ脱炭炉7に導入する。The molten metal is then led to the decarburization furnace 7, but prior to its introduction, pretreated hot metal is added to the decarburization furnace 7.
この脱炭炉7では、上方から延長されているランス8に
より酸素を供給すると共に、炉の下部の羽口9からは酸
素と希釈用アルゴンを吹き上げるようにしているもので
ある。In this decarburization furnace 7, oxygen is supplied by a lance 8 extending from above, and oxygen and argon for dilution are blown up from a tuyere 9 at the bottom of the furnace.
なお、この脱炭炉7にも発生ガス用排気口9を備九でい
る。Note that this decarburization furnace 7 is also equipped with an exhaust port 9 for generated gas.
なお、当然のことながら、予備処理を行った溶銑は、溶
融還元炉に連続的に装入することもできる。Note that, as a matter of course, the pretreated hot metal can also be continuously charged into the smelting reduction furnace.
この場合、高炭素フェロクロムではなく、クロム濃度の
低いステンレス粗溶rJ5に相当する成分が連続的に出
湯することになる。In this case, instead of high carbon ferrochrome, a component corresponding to crude stainless steel melt rJ5 with a low chromium concentration is continuously discharged.
また、脱ガスがひつうような場合には、脱炭炉または成
分調整用ピットに真空脱ガス機能を備えろことも可能で
ある。In addition, if degassing is necessary, it is also possible to equip the decarburizing furnace or the component adjustment pit with a vacuum degassing function.
図に示したような構成を有する連続精錬設備について、
各種の予備的な検討を行ったうえでステンレスの連続精
錬を行ったところ、50 ’t / 90分の生産を確
保するためには、溶融還元炉としてば20を転炉以下、
脱炭炉として5を転炉以下と、非常にコンバク!・な設
備で十分機能させ得ることを確認した。Regarding continuous refining equipment having the configuration shown in the figure,
After conducting various preliminary studies, we conducted continuous refining of stainless steel, and found that in order to ensure production of 50't/90 minutes, we would need to use a converter or less in the form of a smelting reduction furnace.
As a decarburization furnace, it is less than a converter, making it extremely compact!・We confirmed that the system can function satisfactorily with appropriate equipment.
本発明を実施することにより、従来では極めて大型の設
備を必要とした$1?錬設備に対して、電力を使用する
ことがなく、またクロム源を溶解した状態のまま使用す
ることが可能で、しかも非常にコンパクトな装置であり
ながら従来の装置と同等、もしくはそれ以上の処理能力
を発揮させることを可能とした連続精錬方法とするとと
/i!rJJ能としたものである。By implementing the present invention, $1? The smelting equipment does not require electricity, can use the chromium source in a molten state, and is extremely compact, yet provides processing equivalent to or better than conventional equipment. If it is a continuous refining method that allows you to demonstrate your abilities, /i! rJJ Noh.
図は、本発明の連続精錬法を説明するための概略図であ
る。
1 溶融還元炉、2 供給ランス、3 別途のランス、
4 溶融還元炉下側の羽口4.5 投入口、6 脱ガス
用排気口、7 脱炭炉、8 脱炭炉のランス、9・脱炭
炉下部の羽口。The figure is a schematic diagram for explaining the continuous refining method of the present invention. 1 Melting reduction furnace, 2 Supply lance, 3 Separate lance,
4. Tuyere on the lower side of the smelting reduction furnace 4.5 Inlet, 6. Exhaust port for degassing, 7. Decarburization furnace, 8. Lance of the decarburization furnace, 9. Tuyere on the lower side of the decarburization furnace.
Claims (1)
部に設けた羽口、炉内に設置したランスのいずれか一方
あるいはその両方から酸素を溶銑に吹き込んで鉱石を還
元精錬する方式において、溶融還元炉と脱炭炉とを連結
させ、溶融還元炉ではランスから酸素ガスを供給し、炉
下部羽口から酸素および窒素またはアルゴンの少なくと
も一方のガスを吹き込むと共に、鉱石、炭材および石灰
のフラックスをこれらガスと共にあるいは単独に供給し
て鉱石と炭材を上部から供給する一方、ランスからは酸
素を供給して還元反応を行わせ、ここから送り出される
溶湯に予備処理溶銑を添加しつつ、連続的にこれを脱炭
炉に導き、ここでランスから酸素を、またアルゴン、窒
素および酸素のうちの一種以上のガスを主成分とするガ
スを炉下部羽口から吹き込んで脱炭反応と成分調整を行
なわせることからなる連続精錬方法。A method in which ore, carbonaceous materials, and lime are added to hot metal in a smelting furnace, and oxygen is blown into the hot metal from either or both of the tuyere installed at the bottom of the furnace and the lance installed inside the furnace to reduce and smelt the ore. In this method, a smelting reduction furnace and a decarburization furnace are connected, and in the smelting reduction furnace, oxygen gas is supplied from a lance, and at least one of oxygen and nitrogen or argon gas is blown from a tuyere in the lower part of the furnace. Lime flux is supplied together with these gases or alone, and ore and carbonaceous materials are supplied from the top, while oxygen is supplied from the lance to carry out a reduction reaction, and pre-treated hot metal is added to the molten metal sent from here. At the same time, it is continuously guided to a decarburization furnace, where oxygen is blown from a lance and gas mainly composed of one or more of argon, nitrogen, and oxygen is blown from the tuyere at the bottom of the furnace to carry out the decarburization reaction. A continuous refining method that consists of adjusting the ingredients.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19935885A JPS6260813A (en) | 1985-09-11 | 1985-09-11 | Continuous refining method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19935885A JPS6260813A (en) | 1985-09-11 | 1985-09-11 | Continuous refining method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6260813A true JPS6260813A (en) | 1987-03-17 |
Family
ID=16406432
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19935885A Pending JPS6260813A (en) | 1985-09-11 | 1985-09-11 | Continuous refining method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6260813A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02232312A (en) * | 1989-03-07 | 1990-09-14 | Kawasaki Steel Corp | Method for producing stainless steel |
| JPH052186U (en) * | 1991-06-19 | 1993-01-14 | 小野産業株式会社 | Magnetic display device |
| KR100384119B1 (en) * | 1996-07-29 | 2003-08-21 | 주식회사 포스코 | Refining method of low carbon, low nitrogen stainless steel |
-
1985
- 1985-09-11 JP JP19935885A patent/JPS6260813A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02232312A (en) * | 1989-03-07 | 1990-09-14 | Kawasaki Steel Corp | Method for producing stainless steel |
| JPH052186U (en) * | 1991-06-19 | 1993-01-14 | 小野産業株式会社 | Magnetic display device |
| KR100384119B1 (en) * | 1996-07-29 | 2003-08-21 | 주식회사 포스코 | Refining method of low carbon, low nitrogen stainless steel |
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