JP3345622B2 - Hot metal pretreatment method - Google Patents
Hot metal pretreatment methodInfo
- Publication number
- JP3345622B2 JP3345622B2 JP25390092A JP25390092A JP3345622B2 JP 3345622 B2 JP3345622 B2 JP 3345622B2 JP 25390092 A JP25390092 A JP 25390092A JP 25390092 A JP25390092 A JP 25390092A JP 3345622 B2 JP3345622 B2 JP 3345622B2
- Authority
- JP
- Japan
- Prior art keywords
- hot metal
- cao
- desulfurization
- flux
- slag
- 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 - Fee Related
Links
Landscapes
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は溶銑の予備処理方法に係
り、特に脱珪、脱りん後にMg系フラツクスを使用して
有効に脱硫を行う溶銑の予備処理方法に関し、製鋼分野
に広く利用される。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for pretreatment of hot metal, and more particularly to a method for pretreatment of hot metal in which desulfurization and dephosphorization are carried out effectively using Mg-based flux after desiliconization and dephosphorization, and is widely used in the steelmaking field. You.
【0002】[0002]
【従来の技術】高炉から出銑した溶銑を混銑車等の容器
に収容し、ランスを介して不活性ガスで気送し、それぞ
れ異なるフラツクスを溶銑中に吹込んで脱珪、脱りん、
脱硫する予備処理は広く実施されている。一般に金属M
gは優れた脱硫能力を有することが知られており、Mg
単独もしくはCaOとの混合組成物が脱硫剤として用い
られている。しかし従来金属Mgを脱硫剤として使用す
る上に、次の如き問題点があつた。 (イ) Mgの価格が高く、脱硫に要するコストが高くな
る。 (ロ) 沸点が低く蒸気圧が高いため、高温になるほど反
応効率が低くなる。 (ハ) Mg系フラツクスによる溶銑の脱硫においては、
生成したMgSが次の(1)式による反応により、MgO
とSになり易いために処理後復硫が生じ易い。 MgS十(O)→MgO十S……………………(1) 更に溶銑中の酸素もしくはスラグ中のFeOとフラツク
ス中のMgが(1)式により反応し易いので、吹込んだ
高価なMgが脱硫に有効に利用されないという問題点が
あつた。2. Description of the Related Art Hot metal spouted from a blast furnace is housed in a container such as a mixed iron car, and is blown with inert gas through a lance, and different fluxes are blown into the hot metal to desiliconize, dephosphorize,
Pretreatment for desulfurization is widely practiced. Generally metal M
g is known to have excellent desulfurization ability,
A single composition or a mixed composition with CaO is used as a desulfurizing agent. However, there have been the following problems in addition to the conventional use of metallic Mg as a desulfurizing agent. (B) The price of Mg is high, and the cost required for desulfurization increases. (B) Since the boiling point is low and the vapor pressure is high, the higher the temperature, the lower the reaction efficiency. (C) In the desulfurization of hot metal with Mg-based flux,
The generated MgS reacts with the following formula (1) to form MgO.
And S, the resulfurization after the treatment is liable to occur. Since MgS ten (O) → MgO ten S ........................ (1) further Mg oxygen or FeO and in Furatsukusu in the slag in the hot metal (1) tends to react by expression expensive forme blowing There is a problem that Mg is not effectively used for desulfurization.
【0003】その結果、従来は高炉スラグが少量しか存
在しない溶銑、すなわち、脱珪、脱りん処理をしない場
合の溶銑にのみ利用されていたに過ぎず、また脱硫処理
後でもS≦0.005%は得られなかつた。また、Mgと
CaOの混合粉をインジエクシヨンすることにより、M
gの脱硫反応効率が向上することが知られている。しか
し、MgとCaOを同時にインジエクシヨンするか、溶
銑に直接添加するので、スラグの組成CaO/SiO2を
適度に調整することができず、更に上記(1)式による
生成(MgS)がスラグの酸素の存在による復硫のほ
か、脱りん処理後のスラグ中のFeOにより復りんが発
生し易いという問題があつた。[0003] As a result, hitherto, the blast furnace slag has conventionally been used only for hot metal in which only a small amount of slag is present, that is, hot metal in the case where desiliconization and dephosphorization are not performed, and S ≦ 0.005 even after desulfurization. % Was not obtained. Further, by injecting a mixed powder of Mg and CaO, M
It is known that the efficiency of the desulfurization reaction of g is improved. However, since the Mg and CaO are simultaneously infused or added directly to the hot metal, the composition of the slag CaO / SiO 2 cannot be adjusted appropriately, and furthermore, the generation (MgS) of the slag by the above formula (1) is caused by oxygen of the slag. In addition to resulfurization due to the presence of sulfur, there is a problem that rephosphorization easily occurs due to FeO in the slag after the dephosphorization treatment.
【0004】[0004]
【発明が解決しようとする課題】Mgフラツクスは脱硫
にすぐれた効果が認められているものの、従来の脱りん
と脱硫を同時に進行させる方法では、上記の如き多くの
問題点があり、更に原単位の上昇による費用の高騰と、
溶銑への復硫という2つの大きな問題があつた。本発明
の目的は、上記従来技術の課題を解決し、特に復硫を防
止し、Mg系フラツクスの反応効率を向上させることが
できる溶銑の予備処理方法を提供しようとするものであ
る。Although the Mg flux has been found to have an excellent effect on desulfurization, the conventional method for simultaneously proceeding dephosphorization and desulfurization has many problems as described above, and furthermore, has a problem in terms of the basic unit. Soaring costs,
There were two major problems: resulfurization of hot metal. SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems of the prior art, and particularly to provide a pretreatment method for hot metal that can prevent resulfurization and improve the reaction efficiency of Mg-based flux.
【0005】[0005]
【課題を解決するための手段】本発明の要旨とするとこ
ろは次の如くである。 (1)混銑車等の容器に収容された溶銑にフラツクスを
吹込んで脱珪、脱りん、脱硫等を行う溶銑の予備処理方
法において、フラツクスを吹込んで脱珪、脱りんを行い
その後除滓する段階と、CaOを含有するフラツクスを
溶銑中に吹込むか、もしくは該フラツクスを溶銑上に添
加してスラグの塩基度CaO/SiO2≧2.0に調整す
る段階と、前記溶銑に金属MgおよびCaOを含む粉体
脱硫剤をフラツクスとしてガス吹込みを行うか、もしく
は該粉体脱硫剤を溶銑上に添加する段階と、前記溶銑中
に気体を吹込みバブリング撹拌を行う段階と、を有して
成ることを特徴とする溶銑の予備処理方法。 (2)前記粉体脱硫剤は金属Mg:5〜50重量%、C
aO:95〜50重量%を含有することを特徴とする上
記(1)に記載の溶銑の予備処理方法。The gist of the present invention is as follows. (1) In a pretreatment method of molten iron in which flux is blown into a molten iron housed in a container such as a mixed iron car to perform desiliconization, dephosphorization, desulfurization, etc., the flux is blown to desiliconize and dephosphorize, and then dedusting A step of injecting a flux containing CaO into the hot metal or adding the flux onto the hot metal to adjust the slag basicity to CaO / SiO 2 ≧ 2.0; A step of injecting gas using a powder desulfurizing agent containing CaO as a flux, or adding the powder desulfurizing agent to hot metal, and a step of injecting gas into the hot metal and performing bubbling stirring. A method for pretreating hot metal, comprising: (2) The powder desulfurizing agent is metallic Mg: 5 to 50% by weight, C
aO: 95 to 50% by weight is contained, the hot metal pretreatment method according to the above (1),
【0006】本発明の詳細を添付図面を参照して説明す
る。先ず、通常の酸化鉄と石灰の混合フラツクスを溶銑
に吹込んで、脱珪と脱りんを行う。次ぎに脱珪、脱りん
スラグを除滓する。次ぎに脱硫処理に先立つてスラグの
塩基度CaO/SiO2の調整を行う。すなわち、CaO
を含有するフラツクスを溶銑中に吹込むか、もしくはC
aOを溶銑上に添加してCaO/SiO2≧2.0に調整
する。図1は本発明者らが行つたMgフラツクスの脱硫
反応効率を塩基度1.0〜4.0と変化させて調査した
結果である。すなわち、Mg系フラツクスの脱硫反応効
率はCaO/SiO2>1の領域において急激に向上し、
塩基度CaO/SiO2=4まで上昇を継続するが、脱硫
反応効率を少くとも35%に確保するためにはCaO/
SiO2≧2であることを要する。また本発明者らは、ス
ラグの塩基度と脱硫処理中の復りん量の関係を調査した
ところ図2を得た。すなわち、スラグの塩基度CaO/
SiO2<2の場合には脱硫処理中に復りんする現象が発
生した。この復りんを防止するためにはCaO/SiO2
≧2であることを要する。以上2つの大きな理由によつ
て、本発明においては脱硫処理前において塩基度CaO
/SiO2≧2に調整することを必須要件として限定し
た。The details of the present invention will be described with reference to the accompanying drawings. First, a mixed flux of ordinary iron oxide and lime is blown into hot metal to perform desiliconization and dephosphorization. Next, desiliconization and dephosphorization slag are removed. Next, the basicity of the slag CaO / SiO 2 is adjusted prior to the desulfurization treatment. That is, CaO
Is injected into the hot metal, or
aO is added to the hot metal to adjust CaO / SiO 2 ≧ 2.0. FIG. 1 shows the results of an investigation carried out by the present inventors by changing the desulfurization reaction efficiency of Mg flux to a basicity of 1.0 to 4.0. That is, the desulfurization reaction efficiency of the Mg-based flux is sharply improved in the region of CaO / SiO 2 > 1,
The basicity continues to rise to CaO / SiO 2 = 4, but in order to secure the desulfurization reaction efficiency to at least 35%, CaO /
It is necessary that SiO 2 ≧ 2. The present inventors also investigated the relationship between the basicity of the slag and the amount of rephosphorization during the desulfurization treatment, and obtained FIG. That is, the basicity of slag CaO /
In the case of SiO 2 <2, a phenomenon of phosphorus reversion during desulfurization treatment occurred. In order to prevent this rephosphorization, CaO / SiO 2
≧ 2. For the above two major reasons, in the present invention, the basicity of CaO
Adjustment to / SiO 2 ≧ 2 is limited as an essential requirement.
【0007】次に本発明による金属MgとCaOとの混
合組成物による粉体脱硫剤の配合割合について説明す
る。この組成割合は溶銑中のS含有量と、目標とする脱
硫量により異なり、 金属Mg: 5〜50重量% CaO量:95〜50重量% とし、高価なMgの最小限の使用量による最大限の反応
効率を目標として配合割合を決定する。なお、本発明に
よる金属MgとCaOとの粉体脱硫剤による脱硫処理に
おいては、常に溶銑中に気体を吹込みバブリング撹拌を
行う。これは吹込みもしくは溶銑上へ添加した粉体脱硫
剤が溶銑中に均一に混合して反応効率を向上させるため
に必要な条件であつて、この気体吹込みによるバルリン
グ撹拌によりMg系フラツクスの反応効率を著しく向上
させることができた。Next, the mixing ratio of the powder desulfurizing agent in the mixed composition of metallic Mg and CaO according to the present invention will be described. The composition ratio varies depending on the S content in the hot metal and the target desulfurization amount. Metal Mg: 5 to 50% by weight CaO amount: 95 to 50% by weight, and the maximum by the minimum amount of expensive Mg The mixing ratio is determined with the aim of the reaction efficiency of the reaction. In the desulfurization treatment of the metal Mg and CaO with the powder desulfurizing agent according to the present invention, gas is always blown into the hot metal to perform bubbling stirring. This is the condition required to improve the reaction efficiency by uniformly mixing the powder desulfurizing agent injected into or into the hot metal to improve the reaction efficiency. Efficiency could be significantly improved.
【0008】[0008]
【作用】本発明によればMg系フラックスのインジエク
シヨンもしくは溶銑上に添加することによる脱硫処理を
行う前に、CaOのインジエクシヨンもしくはスラグへ
の添加により、スラグの塩基度CaO/SiO2を調整
し、これを2.0以上とする前処理を施したので、スラ
グの流動性が悪化し、ほとんど固化する程度となるので
Mgが酸化されにくくなり、 MgS十(O)→MgO十S なる(1)式の反応が抑制され、Mgが有効に反応する
ようになる。 また、MgS十CaO→CaS十MgO………………(2) なる(2)式の反応が促進されるので、より安定なCa
Sとなつてスラグ中に吸収され、脱硫が達成される。According to the present invention, before performing desulfurization treatment by adding Mg-based flux to indie or hot metal, the basicity of slag CaO / SiO 2 is adjusted by adding CaO to indie or slag. since it subjected to a treatment prior to this a 2.0 or more, and deterioration in fluidity of the slag, Mg is less likely to be oxidized since a degree that almost solidified, MgS ten (O) → become MgO ten S (1) The reaction of the formula is suppressed, and Mg reacts effectively. Further, since the reaction represented by the following formula (2) is promoted: MgS-> 10 CaO → CaS-> MgO (2)
As S is absorbed in the slag, desulfurization is achieved.
【0009】[0009]
実施例1 高炉から出銑された溶銑の成分は次の如くであつた。 C Si Mn P S 4.55重量% 0.18 0.27 0.130 0.025 この溶銑を混銑車内で酸化鉄と石灰の混合フラツクスに
て脱珪、脱りん処理した後の溶銑成分は次のごとくであ
つた。 C Si Mn P S 4.55重量% 0.01 0.20 0.040 0.022 この脱珪、脱りんスラグを混銑車を傾動して除滓した。
混銑車の残存スラグ上にCaOを添加し、塩基度CaO
/SiO2≧2.0の2.8とした後、(金属Mg30重量%
十CaO70重量%)の混合フラツクスを溶銑中に吹込
んで脱硫処理を行つた。脱硫後のS含有量は0.005
%であつた、この脱硫処理中に復りんは全く認められ
ず。また塩基度2.8におけるMg系フラックスの反応効
率は43%であつた。Example 1 The components of the hot metal spiked from the blast furnace were as follows. C Si Mn P S 4.55% by weight 0.18 0.27 0.130 0.025 The hot metal after desiliconization and dephosphorization of this hot metal with a mixed flux of iron oxide and lime in a mixed iron car is as follows: It was like C Si Mn PS 4.55% by weight 0.01 0.020 0.040 0.022 The desiliconized and dephosphorized slag was sludge-removed by tilting a mixed iron wheel.
CaO is added to the remaining slag of the mixed iron wheel, and the basicity is CaO.
/ SiO 2 ≧ 2.0 and 2.8 (metal Mg 30% by weight)
(A 70% by weight of CaO) was blown into the hot metal to perform a desulfurization treatment. The S content after desulfurization is 0.005.
%, No rephosphorization was observed during this desulfurization treatment. The reaction efficiency of the Mg-based flux at a basicity of 2.8 was 43%.
【0010】実施例2 Mg金属とCaOとの混合フラックスによる単なる吹込
みを行う従来法と、脱硫処理前にCaOを含むフラック
スを吹込むか、もしくは溶銑上にCaOを添加して塩基
度CaO/SiO2≧2.0とする前処理を施した後、
脱硫処理する本発明法とのMg系フラックス使用量と溶
銑中のS含有量の推移とを対比する比較試験を行った。
結果は図3に示すとおりである。図3から明らかな如
く、S=0.025%の溶銑を脱硫して0.005%の
S濃度にする場合、FeS+Mg=MgS+Feに従い
脱硫が行われるが、従来は理論計算量の約4倍のMgを
消費しており、上記の場合0.2kg/tのSを脱硫す
るために0.2×(24.30/32.06)×4=
0.60kg/tのMg金属を要していたが、本発明に
おいては2.2〜2.5倍すなわち、0.2×(24.
30/32.06)×2.2=0.33kg/tないし
0.2×(24.30/32.06)×2.5=0.3
8kg/tのMg金属で足りる。従って、反応効率を従
来の25〜30%から40〜45%へと著しく向上させ
ることができた。Example 2 A conventional method of simply blowing with a mixed flux of Mg metal and CaO, a method of blowing a flux containing CaO before desulfurization treatment, or adding CaO onto hot metal to add a basicity of CaO / After performing a pretreatment to make SiO 2 ≧ 2.0,
A comparative test was conducted to compare the amount of Mg-based flux used with the method of the present invention to be desulfurized and the transition of the S content in the hot metal.
The results are as shown in FIG. As is clear from FIG. 3, when the S concentration of 0.005% by desulfurizing S = 0.025% in the hot metal, according FeS + Mg = MgS + Fe
Although desulfurization is performed, conventionally has consumes about four times the Mg theoretical calculated amount, to desulfurize the S of the above cases 0.2 k g / t
0.2 × For that (24.30 / 32.06) × 4 =
Although 0.60 kg / t of Mg metal was required, in the present invention, it was 2.2 to 2.5 times, that is, 0.2 × (24.
30 / 32.06) × 2.2 = 0.33 kg / t or
0.2 × (24.30 / 32.06) × 2.5 = 0.3
8 kg / t of Mg metal is sufficient. Therefore, the reaction efficiency could be significantly improved from the conventional 25-30 percent to 40-45 percent.
【0011】[0011]
【発明の効果】本発明による溶銑の予備処理方法、特に
脱硫方法は、脱珪、脱りん処理を終了した溶銑のスラグ
を除滓した後、Mg系フラックスによる脱硫処理に先立
つて、CaOを含むフラツクスをインジエクシヨンする
か、もしくは溶銑上に添加してスラグの塩基度CaO/
SiO2≧2に調整した後、Mg系フラックスにて脱硫
し、この脱硫処理中は不活性ガスを溶銑中に吹込んでバ
ブリング撹拌を行うことにより次の如き効果を挙げるこ
とができた。 (イ)従来法よりもMgの脱硫効率を著しく向上させる
ことができた。 (ロ)従来脱硫処理中に見られた復りん現象は全く見ら
れず、完全に防止することができた。According to the pretreatment method of the present invention, particularly desulfurization method, the slag of the hot metal which has been subjected to the desiliconization and dephosphorization treatment is subjected to slag removal and then contains CaO prior to the desulfurization treatment with Mg-based flux. Influx the flux or add it to the hot metal to add the basicity of slag CaO /
After adjusting to SiO 2 ≧ 2, desulfurization was performed with Mg-based flux. During this desulfurization treatment, an inert gas was blown into the hot metal and subjected to bubbling stirring to obtain the following effects. (A) The desulfurization efficiency of Mg was significantly improved as compared with the conventional method. (B) The rephosphorization phenomenon conventionally observed during the desulfurization treatment was not observed at all and could be completely prevented.
【図1】本発明によるMg系フラックスによる脱硫処理
に先立つて、スラグの塩基度CaO/SiO2≧2.0に
調整することにより、Mg系フラックス反応効率が塩基
度の上昇に従つて向上することを示す相関線図である。FIG. 1 Prior to desulfurization treatment with Mg-based flux according to the present invention, by adjusting the basicity of slag to CaO / SiO 2 ≧ 2.0, the Mg-based flux reaction efficiency is improved as the basicity increases. FIG.
【図2】Mg系フラックスによる脱硫処理における、ス
ラグの塩基度と復りん、脱りんの関係を示す相関線図で
ある。FIG. 2 is a correlation diagram showing a relationship between basicity of slag and rephosphorization and dephosphorization in desulfurization treatment using a Mg-based flux.
【図3】本発明の実施例におけるMg系フラックスによる
脱硫処理に先立つてスラグの塩基度CaO/SiO2≧
2.0に調整する場合と、スラグの塩基度調整を行わな
い従来法との、溶銑中のS濃度(%)とMg系フラック
ス使用量(Kg/t)との関係を対比する相関線図である。FIG. 3 shows a basicity of slag CaO / SiO 2 ≧ prior to desulfurization treatment with Mg-based flux in an example of the present invention.
Correlation diagram comparing the relationship between the S concentration (%) in hot metal and the amount of Mg-based flux used (Kg / t) between the case of adjusting to 2.0 and the conventional method without adjusting the slag basicity. It is.
フロントページの続き (72)発明者 牧野 光紀 岡山県倉敷市水島川崎通一丁目(番地な し) 川崎製鉄株式会社 水島製鉄所内 (72)発明者 藤村 俊生 岡山県倉敷市水島川崎通一丁目(番地な し) 川崎製鉄株式会社 水島製鉄所内 (56)参考文献 特開 昭63−238209(JP,A) 特開 昭63−86810(JP,A) (58)調査した分野(Int.Cl.7,DB名) C21C 1/00 C21C 1/02 102 C21C 1/02 110 C21C 1/04 101 Continued on the front page (72) Inventor Mitsuno Makino 1-chome, Mizushima-Kawasaki-dori, Kurashiki-shi, Okayama Pref. None) Kawasaki Steel Corporation, Mizushima Works (56) References JP-A-63-238209 (JP, A) JP-A-63-86810 (JP, A) (58) Fields investigated (Int. Cl. 7 , (DB name) C21C 1/00 C21C 1/02 102 C21C 1/02 110 C21C 1/04 101
Claims (2)
ツクスを吹込んで脱珪、脱りん、脱硫等を行う溶銑の予
備処理方法において、フラツクスを吹込んで脱珪、脱り
んを行いその後除滓する段階と、CaOを含有するフラ
ツクスを溶銑中に吹込むか、もしくは該フラツクスを溶
銑上に添加してスラグの塩基度CaO/SiO2≧2.0
に調整する段階と、前記溶銑に金属MgおよびCaOを
含む粉体脱硫剤をフラツクスとしてガス吹込みを行う
か、もしくは該粉体脱硫剤を溶銑上に添加する段階と、
前記溶銑中に気体を吹込みバブリング撹拌を行う段階
と、を有して成ることを特徴とする溶銑の予備処理方
法。1. A pretreatment method for hot metal in which a flux is blown into a hot metal housed in a container such as a mixed-iron car for desiliconization, dephosphorization, desulfurization, etc. Slag and blowing a flux containing CaO into the hot metal, or adding the flux onto the hot metal to add slag basicity CaO / SiO 2 ≧ 2.0
And performing a gas injection using a powder desulfurizing agent containing metallic Mg and CaO to the hot metal as a flux, or adding the powder desulfurizing agent onto the hot metal,
Performing a bubbling agitation by injecting a gas into the hot metal, wherein the hot metal is pre-treated.
量%、CaO:95〜50重量%を含有することを特徴
とする請求項1に記載の溶銑の予備処理方法。2. The method according to claim 1, wherein the powder desulfurizing agent contains 5 to 50% by weight of metal Mg and 95 to 50% by weight of CaO.
Priority Applications (1)
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JP25390092A JP3345622B2 (en) | 1992-08-28 | 1992-08-28 | Hot metal pretreatment method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP25390092A JP3345622B2 (en) | 1992-08-28 | 1992-08-28 | Hot metal pretreatment method |
Publications (2)
Publication Number | Publication Date |
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JPH0681020A JPH0681020A (en) | 1994-03-22 |
JP3345622B2 true JP3345622B2 (en) | 2002-11-18 |
Family
ID=17257648
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JP25390092A Expired - Fee Related JP3345622B2 (en) | 1992-08-28 | 1992-08-28 | Hot metal pretreatment method |
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JP (1) | JP3345622B2 (en) |
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1992
- 1992-08-28 JP JP25390092A patent/JP3345622B2/en not_active Expired - Fee Related
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