JPS609813A - Refining method by increasing blown-out mn in converter - Google Patents

Refining method by increasing blown-out mn in converter

Info

Publication number
JPS609813A
JPS609813A JP11649383A JP11649383A JPS609813A JP S609813 A JPS609813 A JP S609813A JP 11649383 A JP11649383 A JP 11649383A JP 11649383 A JP11649383 A JP 11649383A JP S609813 A JPS609813 A JP S609813A
Authority
JP
Japan
Prior art keywords
converter
slag
blown
steel
blowing
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
JP11649383A
Other languages
Japanese (ja)
Other versions
JPS6235445B2 (en
Inventor
Teruyoshi Hiraoka
照祥 平岡
Yoshiyuki Kasuya
糟谷 義幸
Kaoru Ichikawa
馨 市川
Hiroaki Yamamoto
弘明 山本
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
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP11649383A priority Critical patent/JPS609813A/en
Publication of JPS609813A publication Critical patent/JPS609813A/en
Publication of JPS6235445B2 publication Critical patent/JPS6235445B2/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
    • C21C5/32Blowing from above

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)

Abstract

PURPOSE:To increase blown-out Mn and to decrease the oxygen level in a steel by dephosphorizing the molten iron to be charged into a converter by a preliminary treatment and reducing positively slag at the attenuation period of decarburization reaction in the end period of converter refining. CONSTITUTION:A low P molten iron dephosphorized to a product level by a preliminary treatment is used as the above-described molten metal in the stage of charging the molten iron and ferruginous manganese ore into a converter, performing oxygen blowing and obtaining a steel contg. high blown-out Mn. A powder and granular or lumped C-congt. material is added from above in the attenuation period of decarburization reaction in the end period of converter refining so as to arrive at a slag layer and to reduce the slag layer, thereby restoring Mn. The reduction of P is thus suppressed and the reducing rate of ferruginous manganese ore (MnO) is effectively increased, by which the blown-out Mn is much increased and at the same time oxygen level in the steel is decreased by the reduction of the slag.

Description

【発明の詳細な説明】 本発明は、溶銑予備処理によって成品レベルまで脱Pし
た溶銑を用い且つ転炉スラグを炭素含有物質で還元して
復マンガンを図ることによシ吹止(Mn)を上昇させ、
かつ鋼中酸素レベルを低下させる方法に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention uses hot metal that has been dephosphorized to a finished product level through hot metal pretreatment, and reduces the converter slag with a carbon-containing substance to recover manganese. let it rise;
and a method for reducing oxygen levels in steel.

転炉製鋼法においては、その酸素供給形態によって上吹
き、上底吹き、底吹等があるが、その反/ /%/。
In the converter steel manufacturing process, there are top blowing, top bottom blowing, bottom blowing, etc. depending on the oxygen supply form, but the reverse is / /%/.

応機構の基本は同等であるため、以下上吹き転炉につい
て述べる。純酸素上吹き転炉製鋼法は、転炉上部からラ
ンスを通して純酸素を銑鉄上に吹き込み、そのジェット
の衝突による攪拌力によって反応を促進させ、銑鉄中の
不純物を酸化し、それら酸化物を銑鉄上に存在するスラ
グに吸収させ除去することによって銑鉄から鋼を作る方
法である。
Since the basic converter mechanism is the same, the top-blowing converter will be described below. In the pure oxygen top-blown converter steelmaking method, pure oxygen is blown onto the pig iron through a lance from the top of the converter, and the stirring force generated by the collision of the jets accelerates the reaction, oxidizes impurities in the pig iron, and removes these oxides from the pig iron. This is a method of making steel from pig iron by absorbing and removing the slag present above.

転炉吹錬開始にあたっては、スラグの主成分であるCa
O系の副原料を転炉内に投入し、酸素の吹き込みを行な
う。
At the start of converter blowing, Ca, the main component of slag, is
O-based auxiliary raw materials are introduced into the converter, and oxygen is blown into the converter.

吹錬の進行に伴い、まず銑鉄中のシリコンが優先的に酸
化され(Si02)となる。この(5i02 )が固体
の状態のCaOを溶解し、他の不純物を吸収しうる活性
化したスラグを生成する。この時期には[:Mn’:l
、〔P〕の酸化も進行し、それぞれ(MnO)、(P2
O3)の形となって活性化したスラグに吸収されていく
As blowing progresses, silicon in the pig iron is preferentially oxidized (Si02). This (5i02) dissolves the solid state CaO and produces an activated slag that can absorb other impurities. At this time [:Mn':l
, [P] also progresses, resulting in (MnO) and (P2
It is absorbed into the activated slag in the form of O3).

〔Si〕が優先酸化される時期(いわゆる” St 吹
き″)が終わると、次K (C)の酸化が始まり、吹き
込まれる酸素のほぼ全量が銑鉄中の〔C〕と反応する時
期(脱炭最盛期)を迎える。
After the period in which [Si] is preferentially oxidized (so-called "St blowing"), the next oxidation of K (C) begins, and the period in which almost all of the blown oxygen reacts with [C] in the pig iron (decarburization) reaching its peak).

2− この時期には[:Mn:L [P)等の酸化に寄与する
(Fed)の生成かにぶるため銑鉄及びスラグ中の(M
n)、〔P〕の変化が止まる。
2- During this period, (M
n), [P] stops changing.

脱炭最盛期の末期になると造滓がか々り進行し、均一な
溶融スラグが形成されるように々ると、スラグ中の(M
nO)や(Fed)が還元されて溶鋼中にもどってくる
(Mn:)隆起の現象が見られる。
At the end of the peak decarburization period, the slag progresses rapidly and a uniform molten slag is formed.
A phenomenon of upheaval (Mn:) in which nO) and (Fed) are reduced and returned to the molten steel is observed.

この脱炭速度がおちる時期以降再びFeOの増加に伴う
〔Mn〕、〔P〕の酸化が盛んに行々われ、〔Ca、C
M+1)、(Plの低い鋼の生成に到る。従って転炉精
錬においては、不純物除去の観点から適正なスラグを作
ることが大きなポイントと々る。
After the time when this decarburization rate slows down, the oxidation of [Mn] and [P] is actively carried out again as FeO increases, and [Ca, C
M+1), (results in the production of steel with low Pl. Therefore, in converter refining, it is important to create an appropriate slag from the viewpoint of removing impurities.

低燐鋼(成品〔P′3≦θL3、ことKくθθ/jチ〕
を溶製する場合、従来は燐酸化物CP2(ト))の吸収
除去するCaO系副原料を多量に投入し、又場合によっ
ては吹錬途中に排滓し、それまでに吸収した(P2O3
)を炉外に排出し、新ためてCaO系副原料を投入し、
再び吹錬を行なう(いわゆるダブル・スラグ法)等の方
法がとられている。しかし々からこれらの方法では到達
燐に限界があり、又酸化反応を強力て促進するだめ〔P
〕のみならず、〔Mn〕を増加するために添加した鉄M
n鉱石中の[Mr+]も酸化除去されてしまい、出鋼以
降のMn合金鉄添加量が増大し、従って従来法では〔P
)が低く[Mn:]の高い鋼を得る場合、コスト高とな
っていた。しかも鋼中の酸素レベルが高いために、投入
合金鉄による脱酸生成物が増大し、介在物の増加を来た
していた。
Low phosphorus steel (finished product [P'3≦θL3, also known as θθ/jchi]
When melting P2O3, conventionally a large amount of CaO-based auxiliary raw materials to be absorbed and removed by the phosphorus oxide CP2 (P2O3
) is discharged from the furnace, new CaO-based auxiliary raw materials are introduced,
Methods such as blowing again (the so-called double slug method) are used. However, these methods have a limit to the amount of phosphorus that can be reached, and they do not strongly promote the oxidation reaction [P
] as well as iron M added to increase [Mn].
[Mr+] in the n ore is also removed by oxidation, and the amount of Mn alloy iron added after tapping increases. Therefore, in the conventional method, [P
) is low and [Mn:] is high, the cost is high. Furthermore, due to the high oxygen level in the steel, deoxidation products from the input alloy iron increased, leading to an increase in inclusions.

本発明は、上記の欠点を除去するためになされたもので
、次のβつの構成を要件とするものである。
The present invention was made to eliminate the above-mentioned drawbacks, and requires the following β configurations.

先づ第1は、転炉に装入する溶銑(予備処理して成品レ
ベルまで脱Pした溶銑を炉内に装入することであり、そ
の第2は、転炉精錬末期の脱炭反応減衰期にスラグを積
極的に還元して復Mnを図ることである。
The first step is to charge the hot metal into the converter (hot metal that has been pretreated and dephosphorized to the finished product level). The aim is to actively reduce slag during the period to recover Mn.

本発明者等は、吹錬末期の酸化反応形態に着目し、スラ
グ中の(M n O)を還元し、復マンガンを計る目的
で、この時期に炭素含有物質をスラグに対して添加した
。その結果、酸素との親和力の弱い燐の方が優先的に還
元され、復マンガンは僅少であり、いわゆる低燐高Mn
鋼の溶製上好寸しくないことを確認した。
The present inventors focused on the oxidation reaction form at the final stage of blowing, and added a carbon-containing substance to the slag at this stage for the purpose of reducing (M n O) in the slag and measuring remanganese. As a result, phosphorus, which has a weak affinity for oxygen, is preferentially reduced, and only a small amount of remanganese is produced, so-called low phosphorus and high Mn.
It was confirmed that the steel was not suitable for melting.

そこで本発明では、スラグミニマム状態で脱炭のみ行な
い、吹止〔Mn〕を高める為て鉄マンガン鉱石を添加す
る吹錬において、成品レベルまで脱燐した溶銑を用いる
ととてより、Pの還元を抑え、鉄マンガン鉱石(酸化M
n)の還元率を効率的に上昇せしめて吹止〔Mn〕を一
層高め、同時にスラグ還元により鋼中酸素レベルを低下
できるものであるO 溶銑の事前処理により脱Pする方法は既に公知であるが
、その−例を示せば、例えば脱St後の溶銑浴に気配、
焼結鉱、Cab、 Ca−F2等を添加し攪拌すること
により容易に脱Pすることができる。
Therefore, in the present invention, in the blowing process in which only decarburization is performed in the slag minimum state and ferromanganese ore is added to increase the blowstop [Mn], it is possible to reduce P by using hot metal that has been dephosphorized to the finished product level. ferromanganese ore (M oxide
A method of dephosphorizing O by pre-treatment of hot metal is already known, which can efficiently increase the reduction rate of (n) to further increase the blowout [Mn] and at the same time reduce the oxygen level in the steel through slag reduction. However, to give an example, for example, if there is a presence in the hot metal bath after de-Station,
DeP can be easily removed by adding sintered ore, Cab, Ca-F2, etc. and stirring.

以下π本発明の内容を図面て基づき更に詳細に説明する
The contents of the present invention will be explained in more detail below with reference to the drawings.

第1図(7)、(イ)及び(つ)K1溶銑予備処理によ
り脱燐(CP)=θθ/j%)した溶銑を用いた純酸素
上吹転炉吹錬中の溶鉄中及びスラグ中の成分挙動の一例
を示す。第1図(7)に示す如く、脱炭最盛期を過ぎ、
脱炭酸素効率が低下しはじめる点(CB点)以降には(
イ)に示す如くスラグ中の(Fed)が急激に増加し、
それまでにぶっていた〔Mn〕、〔P〕の酸化が再びお
こり、(?)K示す如く、それまでに鉄マンガン鉱石投
入によシ上昇した溶鉄中の[Mn )が低下し、スラグ
に移行する。この時期に本発明方法に従って、スラグ上
方から炭素含有物質例えば塊状コークスをスラグ中に添
加するとこの酸化物が還元され% (:Mn)が鋼中に
戻る。この場合P含有量の高い通常の溶銑を用いれば、
スラグ中の(P2O3)も高くなり、これが優先的に還
元され、(MnO)の還元が僅少となるが、低P銑を用
いることによりスラグ中の(MnO)の還元が十分に行
なえるものである。
Figure 1 (7), (a) and (ii) In molten iron and slag during pure oxygen top-blowing converter blowing using hot metal dephosphorized (CP) = θθ/j%) by K1 hot metal pretreatment An example of the component behavior of is shown below. As shown in Figure 1 (7), after the peak decarburization period has passed,
After the point at which the decarburization oxygen efficiency begins to decrease (CB point), (
As shown in b), (Fed) in the slag increases rapidly,
The oxidation of [Mn] and [P] that had occurred up until then occurred again, and as shown in (?) Transition. At this stage, according to the method of the present invention, if a carbon-containing substance, such as lump coke, is added to the slag from above the slag, this oxide is reduced and % (:Mn) is returned to the steel. In this case, if ordinary hot metal with high P content is used,
(P2O3) in the slag also increases, and this is preferentially reduced, resulting in a slight reduction of (MnO), but by using low P pig iron, (MnO) in the slag can be sufficiently reduced. be.

炭素含有物質を吹錬の初期及び中期に添加して転炉発生
ガスの増加を計ることは公知の技術であるが、本発明は
上記時期では効果が僅少であり、脱炭最盛期を過ぎた(
08点以降)吹錬末期で行なう。
It is a known technique to add carbon-containing substances in the early and middle stages of blowing to increase the gas generated in the converter, but the present invention has little effect during the above period, and the decarburization peak period has passed. (
08 points and above) Performed at the final stage of blowing.

炭素含有物質としてはコークス、石炭、ピッチ、−乙一 グラファイト、木炭等が選ばれる該炭素源を添加する方
法として副原料口等から投入する場合、転炉の排ガス吸
引と落下による溶鉄中への溶解等の阻害要因があるため
、スラグ層への歩留りの観点から、その粒径は、S%か
ら3θ%程度が好ましい。
Coke, coal, pitch, -Otsuichi graphite, charcoal, etc. are selected as carbon-containing substances.When the carbon source is added through an auxiliary raw material port, etc., it is dissolved into the molten iron by suction of exhaust gas from the converter and falling. Therefore, from the viewpoint of yield in the slag layer, the particle size is preferably about S% to 3θ%.

投入方法としては副原料口からの上方添加あるいはスラ
グへの直接インジェクション等が考えられる0 実施例 10θを転炉において、第1表に示すごとき成分の溶銑
を脱Si後説P及び脱S処理して得た第3表の低P溶銑
を用い、第3表に示すごとき副原料を使用して吹錬を行
なった。
Possible charging methods include upward addition from the auxiliary raw material port or direct injection into the slag. Example 10 In a converter, hot metal having the components shown in Table 1 was subjected to Si-removal P and S-removal treatment. Blowing was carried out using the low P hot metal shown in Table 3 obtained in the above manner and the auxiliary raw materials shown in Table 3.

その結果第9表に示すごとき吹止め時の成分を得た。As a result, the components shown in Table 9 at the time of blow-off were obtained.

本発明によって従来法に比べ約θ/係マンガンの高い低
燐鋼を転炉において溶製することができた。
According to the present invention, a low phosphorus steel having a higher θ/manganese ratio than conventional methods can be produced in a converter.

(1)高炉溶銑成分 第 / 表 (2)転炉容量:純酸素上吹転炉 /θθton(3)
装入溶銑成分 第 2 表 (4)装入溶銑温度: /373’C (5) 副原料使用量 第 3 表 従来法 上記(1)〜(5)の条件で、第β図に示す如き吹錬方
法で実施した。
(1) Blast furnace hot metal composition / Table (2) Converter capacity: Pure oxygen top-blown converter / θθton (3)
Charged hot metal composition Table 2 (4) Charged hot metal temperature: /373'C (5) Amount of auxiliary material used Table 3 Conventional method Under the conditions (1) to (5) above, blowing as shown in Fig. It was conducted using the training method.

本発明方法 上記(1)〜(5)の条件で、第3図に示す如き吹錬方
法で実施した。第3図におけるコークス投入量は7 k
g/T−8である。
Method of the Invention The blowing method as shown in FIG. 3 was carried out under the conditions (1) to (5) above. The amount of coke input in Figure 3 is 7k.
g/T-8.

上記の如〈実施した結果を第7表に示す。The results of the above tests are shown in Table 7.

第7表 吹止め時の溶鋼成分及びスラグ成分Table 7: Molten steel composition and slag composition during blow-stopping

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

第1図(7)(イ)及び((財)は脱炭酸素効率、スラ
グ中及び溶鉄中の成分挙動の一例を示すグラフ、第2図
及び第3図は実施例における従来法及び本発明方法の吹
錬パターンを示す図表である。 節1図 (Yン 吠/番己fシ(b/=〕 (・う7) 第2悶 吹舜(仰
Figure 1 (7) (a) and ((Foundation) are graphs showing examples of decarburization oxygen efficiency and component behavior in slag and molten iron. Figures 2 and 3 are examples of the conventional method and the present invention. This is a chart showing the blowing pattern of the method.

Claims (1)

【特許請求の範囲】[Claims] 転炉内へ溶銑及び含Mn物質を装入して酸素吹錬を行な
い吹止Mn の高い鋼を得るKさいし、上記溶銑として
予備処理によって成品レベルまで脱Pした低P溶銑を用
い、且つ転炉精錬末期の脱炭反応減衰期に粉5粒又は塊
状の炭素含有物質を上方添加してスラグ層に到達せしめ
スラグを還元することによシ復Mnを図ることを特徴と
する転炉における吹止Mn上昇精錬方法。
When hot metal and Mn-containing materials are charged into a converter and oxygen blowing is performed to obtain steel with a high blowout Mn, low P hot metal that has been dephosphorized to a finished product level through preliminary treatment is used as the hot metal, and A blowing furnace in a converter characterized in that five grains or lumps of carbon-containing material are added upward during the decarburization reaction decay period at the end of furnace refining to reach the slag layer and reduce the slag to achieve Mn recovery. Refining method to increase stop Mn.
JP11649383A 1983-06-28 1983-06-28 Refining method by increasing blown-out mn in converter Granted JPS609813A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11649383A JPS609813A (en) 1983-06-28 1983-06-28 Refining method by increasing blown-out mn in converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11649383A JPS609813A (en) 1983-06-28 1983-06-28 Refining method by increasing blown-out mn in converter

Publications (2)

Publication Number Publication Date
JPS609813A true JPS609813A (en) 1985-01-18
JPS6235445B2 JPS6235445B2 (en) 1987-08-01

Family

ID=14688491

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11649383A Granted JPS609813A (en) 1983-06-28 1983-06-28 Refining method by increasing blown-out mn in converter

Country Status (1)

Country Link
JP (1) JPS609813A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5591914A (en) * 1978-12-28 1980-07-11 Sumitomo Metal Ind Ltd Manufacture of manganese steel
JPS55128519A (en) * 1979-03-24 1980-10-04 Sumitomo Metal Ind Ltd Enhancing of steel tapping yield

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5591914A (en) * 1978-12-28 1980-07-11 Sumitomo Metal Ind Ltd Manufacture of manganese steel
JPS55128519A (en) * 1979-03-24 1980-10-04 Sumitomo Metal Ind Ltd Enhancing of steel tapping yield

Also Published As

Publication number Publication date
JPS6235445B2 (en) 1987-08-01

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