JP2002256324A - Method for melting high carbon and high chromium steel - Google Patents

Method for melting high carbon and high chromium steel

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Publication number
JP2002256324A
JP2002256324A JP2001061500A JP2001061500A JP2002256324A JP 2002256324 A JP2002256324 A JP 2002256324A JP 2001061500 A JP2001061500 A JP 2001061500A JP 2001061500 A JP2001061500 A JP 2001061500A JP 2002256324 A JP2002256324 A JP 2002256324A
Authority
JP
Japan
Prior art keywords
blowing
steel
chromium
converter
carbon
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
Application number
JP2001061500A
Other languages
Japanese (ja)
Inventor
Daisuke Takahashi
大輔 高橋
Hisashi Osanai
寿 小山内
Hiroshi Nomura
寛 野村
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.)
JFE Steel Corp
Original Assignee
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP2001061500A priority Critical patent/JP2002256324A/en
Publication of JP2002256324A publication Critical patent/JP2002256324A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a method for melting a high carbon and high chromium steel having low phosphorous concentration and high chromium yield. SOLUTION: When the high carbon and high chromium steel is melted by blowing gaseous oxygen and also charging the chromium source into molten iron held in a converter provided with a top-bottom combined blown function of gas for refining, the refining of the other kinds of steels for cleaning the inside of the converter is performed at >=3 heats before melting the objective high carbon and high chromium steel. Thereafter molten iron subjected to pre- dephosphorization for lowering the phosphorous concentration to not higher than (the target value-0.005 mass%) is charged into the converter and blow- refined without adding slag-making promoter of the slag.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、高炭素・高クロム
鋼の溶製方法に係わり、特に、低燐濃度の高炭素・高ク
ロム鋼をクロムの酸化ロスを抑制して溶製する技術に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for smelting high carbon and high chromium steel, and more particularly to a technique for smelting high carbon and high chromium steel having a low phosphorus concentration while suppressing chromium oxidation loss. .

【0002】[0002]

【従来の技術】高炭素鋼を溶製する技術として、特開昭
57−192211号公報は、上吹転炉における高炭素
鋼吹錬方法を提案している。それは、転炉内に保持した
溶銑に酸素ガスを上吹きして吹錬するに際して、吹錬時
間の経過に応じて酸素ガスを噴射するランスの先端位置
を高める所謂ソフトブローを行い、形成されるスラグの
滓化(溶融状態にする)程度を調整し、溶鋼のスロッピ
ングの発生を抑制しながら、脱燐を行うものである。ま
た、炭素(以下、記号Cで表す)が0.5質量%以上の
高炭素鋼とする場合には、そのC量を鋼中に残存させた
状態で吹錬を終了している。従って、この場合、転炉内
での脱炭反応が最盛期にある時に酸素吹錬を終了するこ
とになるので、以下のような配慮が必要になる。 1)脱燐反応が進行し難いので、その促進のために鉄鉱
石の投入量や形成させるスラグ量を増やし、さらにスラ
グの滓化促進のため蛍石を添加したり、前記ソフトブロ
ーを確実に行う、 2)Cの燃焼による発熱が期待できないばかりでなく、
スラグ量が多くなるので、適正な溶鋼温度を確保のため
多量の熱源(コークス、黒鉛、Fe−Si等)を別途添
加する ところで、高炭素鋼のうちでも、軸受け鋼に代表される
高炭素・高クロム鋼を溶製するには、出鋼時の溶鋼温度
が高くなり過ぎるのを防ぐため、吹錬中期にクロム源
(例えば、フェロクロム、クロム鉱石等)を炉内溶銑に
投入して添加する。しかしながら、前記した特開昭57
−192211号公報記載の高炭素鋼吹錬方法を適用し
て吹錬すると、酸素源である鉄鉱石の投入やスラグ量の
増加、ソフトブローの実施で、生成したスラグ中のFe
Oによりクロムが酸化され、燐濃度が低下しないばかり
でなく、溶鋼へのクロム歩留まりが著しく低下するとい
う問題が生じる。また、該クロムの歩留まりを高めるた
め、吹錬の後半にクロム源を添加すると、その溶け残り
が生じる恐れもある。
2. Description of the Related Art As a technique for producing high carbon steel, Japanese Patent Application Laid-Open No. 57-19221 proposes a high carbon steel blowing method in an upper blowing converter. It is formed by performing a so-called soft blow to raise the tip position of the lance that injects the oxygen gas according to the elapse of the blowing time when blowing the oxygen gas upward on the molten iron held in the converter. Dephosphorization is performed while adjusting the degree of slag slag (making it into a molten state) and suppressing occurrence of slag of molten steel. When carbon (hereinafter, represented by symbol C) is high carbon steel of 0.5% by mass or more, blowing is completed with the carbon content remaining in the steel. Accordingly, in this case, the oxygen blowing is terminated when the decarburization reaction in the converter is at its peak, so the following considerations are required. 1) Since the dephosphorization reaction does not easily proceed, the amount of iron ore introduced and the amount of slag to be formed are increased to promote the dephosphorization reaction. 2) Not only can heat from C combustion not be expected,
Since the amount of slag increases, a large amount of heat source (coke, graphite, Fe-Si, etc.) is separately added to secure an appropriate molten steel temperature. To produce high chromium steel, add a chromium source (eg, ferrochrome, chrome ore, etc.) to the hot metal in the furnace during the middle of blowing to prevent the molten steel temperature during tapping from becoming too high. . However, Japanese Patent Application Laid-Open No.
When the high carbon steel blowing method described in Japanese Patent No. -192211 is applied and blown, the iron ore, which is an oxygen source, is added, the amount of slag is increased, and the soft blasting is performed.
O causes chromium to be oxidized, and not only does the phosphorus concentration not decrease, but also causes a problem that the chromium yield to molten steel is significantly reduced. Further, if a chromium source is added in the latter half of blowing to increase the yield of the chromium, the chromium may be left undissolved.

【0003】[0003]

【発明が解決しようとする課題】本発明は、かかる事情
に鑑み、燐濃度が低く、且つクロム歩留まりが高い高炭
素・高クロム鋼の溶製方法を提供することを目的として
いる。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a high carbon and high chromium steel having a low phosphorus concentration and a high chromium yield in view of the above circumstances.

【0004】[0004]

【課題を解決するための手段】発明者は、上記目的を達
成するため鋭意研究し、その成果を本発明に具現化し
た。
Means for Solving the Problems The inventor conducted intensive research to achieve the above object, and embodied the results in the present invention.

【0005】すなわち、本発明は、ガスの上底吹き機能
を備えた転炉に保持した溶銑に、酸素ガスを吹き込むと
共に、クロム源を投入、吹錬して高炭素・高クロム鋼を
溶製するに際し、対象とする高炭素・高クロム鋼の溶製
前3チャージ以上は、転炉内を清浄にする別鋼種の吹錬
を実施し、その後に燐濃度を(目標値−0.005質量
%)以下に予備脱燐処理した溶銑を前記転炉へ装入し、
蛍石や鉄鉱石のようなスラグの滓化促進剤を添加せずに
吹錬することを特徴とする高炭素・高クロム溶鋼の溶製
方法である。
That is, according to the present invention, oxygen gas is blown into a hot metal held in a converter equipped with a gas top-bottom blowing function, and a chromium source is charged and blown to melt high carbon and high chromium steel. In this case, for the three or more charges before melting the high-carbon / high-chromium steel to be processed, blowing of another steel type to clean the inside of the converter is performed, and then the phosphorus concentration is reduced to (target value-0.005 mass). %) The hot metal preliminarily dephosphorized is charged into the converter,
This is a method for producing high carbon and high chromium molten steel, which comprises blowing without adding a slag-making accelerator such as fluorite or iron ore.

【0006】この場合、前記転炉内を清浄にする別鋼種
の吹錬が、燐濃度が0.02質量%以下の溶銑を用い、
且つ形成させたスラグを吹錬後に全量排滓するものであ
ることが好ましい。また、吹錬中に、下記の各式で定義
する攪拌力(記号ε)を700W/t−steel以上
にして溶鋼を攪拌したり、あるいは、前記クロム源の投
入を、全吹錬期間の40%経過以降に行うのが良い。 ε=ε+ε/10 (1) ε=(28.5QT/W)・log[1+L/1.48] (2) ε=(0.0453Qd/W・x)・u(0,0)・cosξ (3 ) ここで、Q:上吹きガス流量(Nm/min) Q:底吹きガス流量(Nm/min) T:溶鋼温度(K) W:溶鋼重量(t) L:鋼浴深さ(m) x:ランス高さ(m) d:ランスのノズル径(m) u(0,0):該ノズル出口でのガス線速度(m/m
in) cosξ:ノズルの傾斜角(°) 本発明によれば、転炉の事前洗浄を行った後に、予備処
理済みの溶銑を用いて、スラグの未滓化吹錬を実施する
ようにしたので、燐濃度が低く、且つクロム歩留まりが
高い高炭素・高クロム鋼を従来よりコストを高めずに安
定して溶製できるようになる。
In this case, the blowing of another steel type for cleaning the inside of the converter uses hot metal having a phosphorus concentration of 0.02% by mass or less,
In addition, it is preferable that the formed slag is entirely discharged after blowing. During the blowing, the molten steel was stirred at a stirring power (symbol ε) defined by the following equations of 700 W / t-steel or more, or the chromium source was charged for 40 minutes during the entire blowing period. It is better to do it after the passage of%. ε = ε B + ε T / 10 (1) ε B = (28.5Q B T / W) · log [1 + L / 1.48] (2) ε T = (0.0453Q T d / W · x) · u 2 (0,0) · cos 2 ξ (3) where, Q T : top blowing gas flow rate (Nm 3 / min) Q B : bottom blowing gas flow rate (Nm 3 / min) T: molten steel temperature (K) W: molten steel weight (t) L: steel bath depth (m) x: lance height (m) d: lance nozzle diameter (m) u 2 (0,0): gas linear velocity at the nozzle outlet ( m / m
in) cos 2 ξ: Nozzle inclination angle (°) According to the present invention, after pre-cleaning of the converter, pre-treated hot metal is used to perform slag-free blowing of slag. As a result, a high-carbon / high-chromium steel having a low phosphorus concentration and a high chromium yield can be stably produced without increasing the cost as compared with the conventional method.

【0007】[0007]

【発明の実施の形態】以下、発明をなすに至った考察も
含め、本発明の実施の形態を説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The embodiments of the present invention will be described below, including the considerations that led to the invention.

【0008】高炭素鋼を溶製する場合には、高炭素で酸
素吹錬を停止するので、あまり脱燐が期待できない。そ
のため、一般に、形成されるスラグ量を増やすと共に、
蛍石を添加してスラグを十分に滓化して、溶鋼への復燐
を防止する。
In the case of producing high carbon steel, oxygen blowing is stopped at high carbon, so that much dephosphorization cannot be expected. Therefore, generally, while increasing the amount of slag formed,
Fluorite is added to sufficiently slag the slag to prevent reversion to molten steel.

【0009】そこで、発明者は、復燐の要因を限りなく
排除できれば、脱燐させるためのスラグを多量に形成さ
せる必要がなくなるし、熱源の投入量も削減できると考
えた。また、この場合には、スラグの滓化促進も必要が
ないので、鉄鉱石や蛍石を添加しないでも良い。その結
果、添加したクロムがスラグに酸化吸収されて、クロム
歩留まりの低減も防止できるようになる。そして、この
考えを具体化するためまず復燐の要因を限りなく排除す
ることを検討し、転炉内の清浄化を思いついた。つま
り、転炉内の残存物(付着物も含める)をできるだけ除
去するか、たとえ残存物があっても燐が含まれていない
状態にする。
Therefore, the inventor thought that if the factor of phosphorus reversion could be eliminated as much as possible, it would not be necessary to form a large amount of slag for dephosphorization, and it would be possible to reduce the input amount of the heat source. In this case, since it is not necessary to promote slag slag formation, iron ore or fluorite may not be added. As a result, the added chromium is oxidized and absorbed by the slag, and a reduction in the chromium yield can be prevented. In order to make this idea concrete, we first considered eliminating the causes of phosphorus recovery as much as possible, and came up with the idea of purifying the inside of the converter. That is, the residue (including the adhered matter) in the converter is removed as much as possible, or even if there is a residue, the state is such that phosphorus is not contained.

【0010】本発明では、転炉内の清浄は、如何なる方
法で実施しても良い。対象鋼種を吹錬をする転炉内に燐
が残存しないようにすれば良いからである。しかし、実
際には、前チャージの吹錬が必ず行われるので、その吹
錬を利用するのが合理的である。そこで発明者は、試験
操業を行い清浄化方法を検討した。そして、対象とする
高炭素・高クロム鋼の溶製前3チャージ以上は、燐濃度
が0.02質量%以下の溶銑を用い、且つ形成させたス
ラグを吹錬後に全量排滓するものであるのが好ましいこ
とを見出し、本発明の1要件とした。3チャージ以上と
したのは、それ以下では十分に清浄化ができないからで
ある。また、溶銑の燐濃度が0.02質量%以下でなけ
れば、3チャージで清浄化ができないし、スラグの全量
排滓も必要である。
In the present invention, the inside of the converter can be cleaned by any method. This is because phosphorus should not be left in the converter that blows the target steel type. However, in practice, the blowing of the pre-charge is always performed, so it is reasonable to use the blowing. Therefore, the inventor conducted a test operation and examined a cleaning method. For the three or more charges before melting of the high-carbon / high-chromium steel to be used, hot metal having a phosphorus concentration of 0.02% by mass or less is used, and the formed slag is discharged after the entire slag is blown. Was found to be preferable, and this was regarded as one requirement of the present invention. The reason why the charge is set to three or more is that if the charge is less than three, the cleaning cannot be sufficiently performed. Unless the concentration of phosphorus in the hot metal is 0.02% by mass or less, cleaning cannot be performed with three charges, and the entire amount of slag must be discharged.

【0011】次に、上記考えを実行するには、清浄化さ
れた転炉に、燐濃度を(目標値−0.005質量%)以
下に予備脱燐処理した溶銑を前記転炉へ装入することが
重要で、これを本発明の第2の要件とした。目標値よ
り、0.005質量%低めた溶銑を使用することで、例
えば洗浄して清浄化された転炉であっても生じることの
ある燐汚染の問題が解消され、これによって、高炭素鋼
の溶製であっても、吹錬中に脱燐状態を懸念しながら吹
錬を行う必要がなくなる。また、スラグの滓化促進剤を
添加せずに吹錬するという第3の要件を加えたのは、前
記したように、クロムの酸化ロスを抑制する対策であ
る。
Next, in order to implement the above idea, hot metal preliminarily dephosphorized to a phosphor concentration of (target value-0.005 mass%) or less is charged into the cleaned converter. This is the second requirement of the present invention. By using hot metal 0.005% by mass lower than the target value, for example, the problem of phosphorus contamination that may occur even in a converter which has been cleaned and cleaned can be solved, and thereby, a high-carbon steel It is not necessary to perform blowing while worrying about the state of dephosphorization during blowing. Further, the third requirement that the slag is blown without adding a slag-making accelerator is a measure to suppress the chromium oxidation loss as described above.

【0012】本発明は、以上述べた3つの要件を、ガス
の上底吹き機能を備えた転炉に保持した溶銑に対して、
酸素ガスを吹き込むと共に、クロム源を投入し、通常の
酸素吹錬するにあたり、実行するものである。これによ
り、低燐濃度で、且つクロムの歩留まり高く高炭素・高
クロム鋼が溶製できるようになる。
The present invention satisfies the above three requirements for hot metal held in a converter equipped with a gas top and bottom blowing function.
In addition to injecting oxygen gas, a chromium source is supplied to perform ordinary oxygen blowing. As a result, a high-carbon, high-chromium steel having a low phosphorus concentration and a high chromium yield can be produced.

【0013】また、本発明では、吹錬中に、前記した各
式で定義する攪拌力(記号ε)を700W/t−ste
el以上にして溶鋼を攪拌するのが良い。これによっ
て、スラグ中のFeO濃度が低下し、クロムの酸化ロス
が抑制できるからである。
Further, in the present invention, during the blowing, the stirring force (symbol ε) defined by the above-mentioned equations is set to 700 W / t-ste.
It is better to stir the molten steel at el or higher. Thereby, the FeO concentration in the slag is reduced, and the chromium oxidation loss can be suppressed.

【0014】さらに、本発明では、前記クロム源の投入
を、全吹錬期間の40〜70%に行うのが良い。これに
よって、クロム歩留まりの安定が期待できるからであ
る。なお、40%未満では、高炭素域で吹錬を完了する
にしても酸化ロスが生じ、70%を超える後半の添加で
は、歩留まりが不安定となる。
Further, in the present invention, the chromium source is preferably charged during 40 to 70% of the entire blowing period. This is because the chromium yield can be expected to be stable. In addition, if it is less than 40%, even if the blowing is completed in the high carbon region, an oxidation loss occurs, and if the addition is more than 70% in the latter half, the yield becomes unstable.

【0015】[0015]

【実施例】C:1.01質量%、Cr:1.56質量
%、P:0.015質量%を含有する低Pで、且つ高炭
素・高クロムの溶鋼を溶製した。その際、本発明に係る
溶製方法及び蛍石や鉄鉱石を大量に使用して脱燐する従
来の溶製方法の両方を適用し、それらの実施成績を比較
して本発明の効果を確認した。溶製に用いた容器は、M
gO-C系不定形耐火物で内張りした、生産能力180
トンの上底吹き転炉であり、上吹きは酸素ガス、底吹き
は不活性ガスを吹き込む方式である。操業方法は、炉内
に保持した溶銑に上吹きランスを介して酸素ガスを吹
き、底から不活性ガスを吹き、上吹き酸素ガスにより主
として脱炭反応を起こし、目標炭素濃度に達したら吹錬
を停止して溶鋼を取鍋に出鋼するものである。なお、溶
銑には、溶銑予備処理で脱珪、脱燐及び脱硫したものを
用いる。また、転炉の炉底に設けた羽口を介して溶銑も
しくは溶鋼に不活性ガスを吹き込み、溶鋼の攪拌も行
う。
EXAMPLE A low-P, high-carbon, high-chromium molten steel containing 1.01% by mass of C, 1.56% by mass of Cr, and 0.015% by mass of P was produced. At that time, both the smelting method according to the present invention and the conventional smelting method of dephosphorizing by using a large amount of fluorite or iron ore are applied, and the performances of the present invention are compared to confirm the effect of the present invention. did. The container used for melting was M
gO-C refractory lining, production capacity 180
This is a top-to-bottom blowing converter, in which the top blowing blows oxygen gas and the bottom blowing blows inert gas. The operating method is to blow oxygen gas onto the hot metal held in the furnace through a top-blowing lance, blow an inert gas from the bottom, and mainly cause a decarburization reaction by the top-blown oxygen gas. And stop the molten steel on the ladle. The hot metal used is one that has been desiliconized, dephosphorized and desulfurized in the hot metal pretreatment. Further, an inert gas is blown into hot metal or molten steel through a tuyere provided at the bottom of the converter to stir the molten steel.

【0016】本発明の実施では、まず転炉の洗浄を行う
ため、対象鋼種とは異なる溶鋼を3チャージにわたり溶
製し、吹錬毎に形成されたスラグは全量排出した。ま
た、各チャージで吹錬する溶鋼の目標P濃度は、0.0
18⇒0.016⇒0.013質量%と低下させ、洗浄
の促進を図った。
In the practice of the present invention, first, in order to clean the converter, molten steel different from the target steel type was smelted over three charges, and the entire amount of slag formed at each blowing was discharged. The target P concentration of molten steel blown at each charge is 0.0
18 → 0.016 → 0.013% by mass to promote cleaning.

【0017】この洗浄が終了した転炉に溶銑予備脱燐済
みの溶銑を、連続して3チャージ行った。各チャージで
転炉へ装入した溶銑のP濃度は,それぞれ0.009、
0.007,0.008質量%であった。また、溶鋼の
攪拌強度εは、底吹きガスの助けで、吹錬中723wa
tt/t−steel以上を保持し、また、クロム源に
はフェロクロム(Cr:62質量%、C:8質量%の所
謂高炭素フェロクロム)を用い、全吹錬期間の40〜7
0%の時期に投入した。
The hot metal that had been preliminarily dephosphorized in the hot metal was continuously charged 3 times in the converter after the completion of the washing. The P concentration of the hot metal charged into the converter at each charge was 0.009,
The content was 0.007, 0.008% by mass. Further, the stirring strength ε of the molten steel was 723 wa during the blowing with the help of the bottom blown gas.
tt / t-steel or more is used, and ferrochrome (a so-called high-carbon ferrochrome of 62% by mass of Cr and 8% by mass of C) is used as a chromium source, and 40 to 7 of a total blowing period is used.
It was introduced at the time of 0%.

【0018】従来法と本発明法の操業結果の一例を表1
に示す。なお、両者とも添加したCr量は1.52%相
当量を添加した時の吹錬後の成績である。また、操業成
績をクロム歩留まりで評価し、従来法での値と比較して
図1に示すが、その平均値は約98%となり、従来法に
よる93.5%を大きく上回っていた。さらに、使用す
る熱源量も、図2に示すように、従来法による場合の6
8%程度であった。
Table 1 shows an example of the operation results of the conventional method and the method of the present invention.
Shown in In both cases, the amount of Cr added is the result after blowing when an amount equivalent to 1.52% was added. In addition, the operating results were evaluated in terms of the chrome yield and compared with the values obtained by the conventional method. The results are shown in FIG. 1, and the average value was about 98%, which was much higher than 93.5% obtained by the conventional method. Further, as shown in FIG. 2, the amount of heat source used is 6
It was about 8%.

【0019】[0019]

【表1】 [Table 1]

【0020】[0020]

【発明の効果】以上述べたように、本発明により、燐濃
度が低く、且つクロム歩留まりが高い高炭素・高クロム
鋼を従来よりコストを高めずに安定して溶製できるよう
になる。
As described above, according to the present invention, a high carbon / high chromium steel having a low phosphorus concentration and a high chromium yield can be stably produced without increasing the cost as compared with the conventional method.

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

【図1】クロム源の炉内添加歩留まりを本発明法と従来
法とで比較した図である。
FIG. 1 is a diagram comparing the yield of addition of a chromium source in a furnace between the method of the present invention and the conventional method.

【図2】転炉へ投入する熱源量を本発明法と従来法とで
比較した図である。
FIG. 2 is a diagram comparing the amount of heat source supplied to a converter between the method of the present invention and the conventional method.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 野村 寛 岡山県倉敷市水島川崎通1丁目(番地な し) 川崎製鉄株式会社水島製鉄所内 Fターム(参考) 4K070 AA04 AB06 AB14 AC03 AC23 BA07 BA12 BA20 BB02 BB05 EA21  ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Hiroshi Nomura 1-chome, Mizushima-Kawasaki-dori, Kurashiki-shi, Okayama Pref. BB05 EA21

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 ガスの上底吹き機能を備えた転炉に保持
した溶銑に、酸素ガスを吹き込むと共に、クロム源を投
入、吹錬して高炭素・高クロム鋼を溶製するに際し、 対象とする高炭素・高クロム鋼の溶製前3チャージ以上
は、転炉内を清浄にする別鋼種の吹錬を実施し、その後
に燐濃度を(目標値−0.005質量%)以下に予備脱
燐処理した溶銑を前記転炉へ装入し、蛍石や鉄鉱石のよ
うなスラグの滓化促進剤を添加せずに吹錬することを特
徴とする高炭素・高クロム溶鋼の溶製方法。
An oxygen gas is blown into a hot metal held in a converter equipped with a gas top and bottom blowing function, and a chromium source is charged and blown to melt high carbon and high chromium steel. Blowing of another steel type to clean the inside of the converter is performed for three or more charges before melting of high carbon and high chromium steel, and then the phosphorus concentration is reduced to (target value-0.005 mass%) or less. The molten metal which has been subjected to the pre-phosphorus treatment is charged into the converter, and is blown without adding a slag-forming accelerator such as fluorite or iron ore. Manufacturing method.
【請求項2】 前記転炉内を清浄にする別鋼種の吹錬
が、燐濃度が0.020質量%以下の溶銑を用い、且つ
形成させたスラグを吹錬後に全量排滓するものであるこ
とを特徴とする請求項1記載の高炭素・高クロム溶鋼の
溶製方法。
2. The blowing of another steel type for cleaning the inside of the converter uses hot metal having a phosphorus concentration of 0.020% by mass or less, and discharges all formed slag after blowing. The method for producing a high-carbon, high-chromium molten steel according to claim 1, wherein:
【請求項3】 吹錬中に、下記の各式で定義する攪拌力
(記号ε)を700W/t−steel以上にして溶鋼
を攪拌することを特徴とする請求項1又は2記載の高炭
素・高クロム溶鋼の溶製方法。 ε=ε+ε/10 (1) ε=(28.5QT/W)・log[1+L/1.48] (2) ε=(0.0453Qd/W・x)・u(0,0)・cosξ (3 ) ここで、Q:上吹きガス流量(Nm/min) Q:底吹きガス流量(Nm/min) T:溶鋼温度(K) W:溶鋼重量(t) L:鋼浴深さ(m) x:ランス高さ(m) d:ランスのノズル径(m) u(0,0):該ノズル出口でのガス線速度(m/m
in) cosξ:ノズルの傾斜角(°)
3. The high carbon steel according to claim 1, wherein the molten steel is agitated during blowing by setting the stirring power (symbol ε) defined by the following equations to 700 W / t-steel or more.・ Making method of high chromium molten steel. ε = ε B + ε T / 10 (1) ε B = (28.5Q B T / W) · log [1 + L / 1.48] (2) ε T = (0.0453Q T d / W · x) · u 2 (0,0) · cos 2 ξ (3) where, Q T : top blowing gas flow rate (Nm 3 / min) Q B : bottom blowing gas flow rate (Nm 3 / min) T: molten steel temperature (K) W: molten steel weight (t) L: steel bath depth (m) x: lance height (m) d: lance nozzle diameter (m) u 2 (0,0): gas linear velocity at the nozzle outlet ( m / m
in) cos 2 ξ: Nozzle inclination angle (°)
【請求項4】 前記クロム源の投入を、全吹錬期間の4
0%経過以降に行うことを特徴とする請求項1〜3のい
ずれかに記載の高炭素・高クロム溶鋼の溶製方法。
4. The charging of the chromium source is performed during the entire blowing period.
The method for producing a high-carbon, high-chromium molten steel according to any one of claims 1 to 3, wherein the method is performed after 0% has elapsed.
JP2001061500A 2001-03-06 2001-03-06 Method for melting high carbon and high chromium steel Pending JP2002256324A (en)

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Publication Number Publication Date
JP2002256324A true JP2002256324A (en) 2002-09-11

Family

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Country Status (1)

Country Link
JP (1) JP2002256324A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103131817A (en) * 2011-11-30 2013-06-05 上海梅山钢铁股份有限公司 Converter steelmaking phosphorus reservation smelting method
CN108118115A (en) * 2016-11-28 2018-06-05 宝山钢铁股份有限公司 A kind of method of VD flows smelting high carbon chromium bearing steel

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103131817A (en) * 2011-11-30 2013-06-05 上海梅山钢铁股份有限公司 Converter steelmaking phosphorus reservation smelting method
CN108118115A (en) * 2016-11-28 2018-06-05 宝山钢铁股份有限公司 A kind of method of VD flows smelting high carbon chromium bearing steel

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