JPS6037847B2 - Molten steel refining method - Google Patents

Molten steel refining method

Info

Publication number
JPS6037847B2
JPS6037847B2 JP55048268A JP4826880A JPS6037847B2 JP S6037847 B2 JPS6037847 B2 JP S6037847B2 JP 55048268 A JP55048268 A JP 55048268A JP 4826880 A JP4826880 A JP 4826880A JP S6037847 B2 JPS6037847 B2 JP S6037847B2
Authority
JP
Japan
Prior art keywords
molten steel
ladle
steel
heating
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.)
Expired
Application number
JP55048268A
Other languages
Japanese (ja)
Other versions
JPS56146814A (en
Inventor
喜代美 田口
正之 半明
勝 石川
治良 田辺
健三 山田
務 碓井
芳雄 宮下
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 Engineering Corp
Original Assignee
Nippon Kokan 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 Nippon Kokan Ltd filed Critical Nippon Kokan Ltd
Priority to JP55048268A priority Critical patent/JPS6037847B2/en
Publication of JPS56146814A publication Critical patent/JPS56146814A/en
Publication of JPS6037847B2 publication Critical patent/JPS6037847B2/en
Expired legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Treatment Of Steel In Its Molten State (AREA)

Description

【発明の詳細な説明】 この発明は、短時間で安価に、極めてリン(P)含有量
の少ない銅(低P鋼)を得るための溶鋼の精錬方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for refining molten steel for obtaining copper (low P steel) with an extremely low phosphorus (P) content in a short time and at low cost.

従来、低P鋼を得るための手段として、転炉吹錬法が知
られている。
Conventionally, a converter blowing method has been known as a means for obtaining low P steel.

転炉吹鏡法としては、通常吹鎌法、ソフトブロー法、ダ
ブルスラグ法、および2回出鋼法が知られているが、こ
れらの方法では、溶鋼中のPの含有量を、それぞれ、1
50、10Q80および70(ppm)程度にしか下げ
ることができない。このように、溶鋼のP含有量を下げ
られない理由は、次の通りである。即ち、転炉吹鉄は、
主に脱炭処理時間に支配され、その処理時間が短いから
、低P鋼を得るための十分な脱P処理時間をとることが
できない。また、脱Pのためのスラグボリューム(量)
を多くすると、スラグ噴出等の危険性があり、作業性に
問題があることから、脱Pのためのスラグポリュームに
は制限がある。従って、転炉吹鎌においては、溶鋼のP
含有量を下げることができなかった。そこでこの発明は
、従釆の転炉吹鎌法では得られなかった、きわめて低い
P含有量の銅を得ることができる、溶鋼の精錬方法を堤
供すべくなされたもので、製鋼炉で精錬された溶鋼を、
密閉用蓋を有し、かつその内部にガスを吹込み可能にし
た取鍋に移注し、ついで前記取鍋内溶鋼に精錬用フラッ
クスを添加し、ついで前記取鍋内綾鋼中にその上方から
浸潰した渡洋用ガスを吹込むためのランスから、前記熔
鋼中に礎梓用ガスの吹込みを行なうことによつて、酸化
性ガス雰囲気下で、前記取鍋内溶鋼および前記溶鋼と前
記溶鋼上のスラグとを郷拝し、ついで、前記取鍋内溶鋼
上のスラグに、加熱電極の先端部を浸潰して、前記取鍋
内溶鋼を、鋳造温度、RH処理用温度等の後処理に適し
た所定温度加熱することに特徴を有する。
As the converter blowing mirror method, the ordinary blowing sickle method, soft blowing method, double slug method, and double tapping method are known, but in these methods, the P content in the molten steel is 1
It can only be lowered to about 50, 10Q80 and 70 (ppm). The reason why the P content of molten steel cannot be lowered in this way is as follows. In other words, converter blowing iron is
It is mainly controlled by the decarburization treatment time, and since the treatment time is short, sufficient dephosphorization treatment time cannot be taken to obtain low P steel. In addition, slag volume (amount) for dephosphorization
If the amount is increased, there is a risk of slag blowing out, etc., and there are problems with workability, so there is a limit to the amount of slag polymer for removing P. Therefore, in the converter blow sickle, the P of molten steel is
It was not possible to lower the content. Therefore, this invention was made to provide a method for refining molten steel that can obtain copper with an extremely low P content, which could not be obtained by the converter blowing sickle method. molten steel,
The molten steel is poured into a ladle that has a sealing lid and into which gas can be blown, and then a refining flux is added to the molten steel in the ladle, and then the molten steel is poured into the twill steel in the ladle above it. The molten steel in the ladle and the molten steel and the molten steel are injected into the molten steel from a lance for injecting the molten steel into the molten steel in an oxidizing gas atmosphere. Then, the tip of a heating electrode is immersed in the slag above the molten steel in the ladle, and the molten steel in the ladle is subjected to post-treatment such as casting temperature and RH treatment temperature. It is characterized by heating at a suitable predetermined temperature.

なお、加熱電極による加熱には、電弧加熱、および抵抗
加熱があり、このように、加熱を行なうことの利点とし
ては、製鋼炉の出鋼温度が下げられることである。
Heating by heating electrodes includes electric arc heating and resistance heating, and the advantage of heating in this way is that the tapping temperature of the steelmaking furnace can be lowered.

即ち、第1図に製鋼炉(転炉)の耐火物溶損係数と、そ
の出鋼温度との関係を示す図、および第2図に製鋼炉(
転炉)において得られた素鋼の〔P〕(Pの濃度)とそ
の出鋼温度との関係を示す図からわかるように(両図に
おいて、曲線aは通常吹錬法によるもの、曲線bはダブ
ルスラグ吹錬法によるものを示す)、出鋼温度(ちなみ
にこの発明における出鋼温度は1590〜164び0で
あり、同じく、従来は1650〜17200C程度であ
る)が低いほど、耐火物の溶損係数が低くなり、また〔
P〕が低くなり(従って取鍋における精錬に有利となる
)、さらに、歩留りがよくなる。また、精錬が加熱の前
に行なわれることの利点として、比較的低い温度で精錬
を行なうことができ、従って脱P効率を上げることがで
きることである。
That is, Fig. 1 shows the relationship between the refractory corrosion coefficient of a steelmaking furnace (converter) and its tapping temperature, and Fig.
As can be seen from the diagrams showing the relationship between [P] (P concentration) of raw steel obtained in a converter and its tapping temperature (in both figures, curve a is for the normal blowing method, curve b is The lower the tapping temperature (Incidentally, the tapping temperature in this invention is 1,590 to 1,640C, and the conventional value is about 1,650 to 17,200C), the higher the refractory quality. The erosion coefficient is lower, and [
P] is lower (therefore, it is advantageous for refining in a ladle), and furthermore, the yield is improved. Further, an advantage of performing the refining before heating is that the refining can be performed at a relatively low temperature, and therefore the dephosphorization efficiency can be increased.

たとえば、第3図に精錬用フラックスとして、メタケィ
酸ソーダを溶鋼1トン当り20k9用いたときの脱P率
と熔鋼温度との関係を示す。さらに、加熱のみが行なわ
れる(即ち、精錬処理と加熱処理とが分離している)こ
との利点として、取鍋内溶鋼面変動が少ない(溶鋼およ
び港鋼とスラグとの精錬による蝿梓が行なわれていない
から)から、加熱が安定に行なえ、しかも、電極榛の長
寿命化が図れることが挙げられる。なお、周知のように
、加熱電極による加熱を行なう際に、取鍋内港鋼中にそ
の上方から浸潰したランスから、加熱促進のためのガス
(日、S等の不純物が鋼中に入らないガス、例えば02
、ふガス等)を、溶鋼中に吹込んで、港鋼を澄拝して加
熱電極による加熱効率を向上させる(その吹込量は、鋼
ITon当り0.4N〆′mjn以下4Nそ′min禾
満が好ましい。その理由は0.4NZ/min未満では
加熱に時間がかかって加熱効率の点からは実用的でなく
なるからであり、一方4Nそ′min以上では溶鋼飛散
によつて地金が電極に付着して電極寿命が短かくなるか
らである。)。また、加熱電極は、加熱晩冬了後、上昇
させて、その先端部を取鍋内スラグから離間させる。ラ
ンスからの、損梓用ガス(日、S等の不純物が鋼中に入
らないガス、例えば02、〜ガス等)流量は、精錬効率
が下らないようにするという点からは、鋼ITon当り
4N〆′min以上であることが好ましく、ガス吹込に
より溶鋼面が上昇しすぎて、いわゆる取鍋内のフリーボ
ードを大きくしなければならず実用的でなくなるという
点からは、鋼ITon当り20Nそ/min以下である
ことが好ましい(なお、このように大きなガス吹込量は
溶鋼の上方から漆鋼中に浸簿するランス構造によっては
じめて得ることができる。
For example, FIG. 3 shows the relationship between the dephosphorization rate and the molten steel temperature when 20 k9 of sodium metasilicate is used per ton of molten steel as a refining flux. Furthermore, the advantage of only heating being performed (that is, the refining process and heat treatment are separated) is that there is less variation in the surface of the molten steel in the ladle. Since the heating is not carried out in the same manner as above), heating can be carried out stably and the life of the electrode combs can be extended. As is well known, when heating with a heating electrode, impurities such as gas (sulfur, sulfur, etc.) to promote heating enter the steel from the lance submerged into the steel in the ladle from above. No gas, e.g. 02
, fugas, etc.) is injected into the molten steel to clear the port steel and improve the heating efficiency by the heating electrode (the amount of injection is 0.4N per ton of steel or less than 4N min). The reason for this is that if the heating rate is less than 0.4 NZ/min, it will take a long time to heat, making it impractical from the point of view of heating efficiency.On the other hand, if the heating rate is 4 N NZ/min or more, the base metal will become attached to the electrode due to molten steel scattering. (This is because it will adhere and shorten the life of the electrode.) Further, after heating is completed in late winter, the heating electrode is raised to separate its tip from the slag in the ladle. From the point of view of not reducing refining efficiency, the flow rate of waste gas (a gas that does not allow impurities such as S, S, etc. to enter the steel, such as 02 gas, etc.) from the lance is 4N per Iton of steel. It is preferable that the molten steel surface rises too much due to gas injection, making it impractical to make the so-called free board in the ladle large. (note that such a large amount of gas blown can only be obtained with a lance structure in which the molten steel is immersed into the lacquered steel from above).

)。ランスからの溶鋼中へのガスの噴出態様は、水平に
対して上下方向にそれぞれ1yの範囲内であることが好
ましい。これはランスから噴出したガスが、まず水平に
広がり、次いで、垂直に上昇するため、溶鋼中に吹込ま
れたガスがきわめて有効に縄梓利用され、高い蝿洋効率
が得られるからである。また、そのためのランスのガス
流通路の形状は、縦断面からみて、凝梓態様を示す第4
図イに示すようなランス1の先端部2箇所に噴出孔la
が位置する、T字2孔型のもの、および同第4図口に示
すようなランス1′の先端部1箇所に噴出孔1′aが位
置する、L字1孔型のものが好ましい。このようなラソ
ス使用によって、図示されるように、溶鋼を取鋼の側壁
からその中心に向けて流動させることができるためスラ
グと鋼浴の蝿洋混合が鋼裕表面に対して均一にかつ鋼浴
深く行なわれ、電極加熱後に添加した精錬用フラックス
は、ランスからのガス擬拝によると溶鋼とも接触混合で
容易に蓬化し、従って蓬化のための電極加熱は必要でな
くなる。また短時間で蓮化したフラックス(スラグ)は
引き続いて溶鋼と激しく接触混合するため、スラグーメ
タル反応が迅速に進行し、高い精錬能が得られる。第5
図イ,口は、この発明を実施するための取鋼の一例を示
す断面図であり、第5図イは加熱電極による加熱態様を
示し、第5図口はランスによる精錬態様を示している。
). The manner in which the gas is ejected from the lance into the molten steel is preferably within a range of 1y in the vertical direction with respect to the horizontal direction. This is because the gas ejected from the lance first spreads horizontally and then rises vertically, so the gas blown into the molten steel is utilized extremely effectively and high efficiency is achieved. In addition, the shape of the gas flow passage of the lance for this purpose is a fourth shape that shows a condensation mode when viewed from the longitudinal section.
There are two spout holes la at the tip of the lance 1 as shown in Figure A.
It is preferable to use a T-shaped two-hole type in which a hole is located, and an L-shaped one-hole type in which an ejection hole 1'a is located at one point at the tip of a lance 1' as shown in the opening of FIG. By using such a lasso, as shown in the figure, the molten steel can be made to flow from the side walls of the steel toward the center, so that the slag and steel bath are mixed uniformly on the steel surface and The refining flux, which is carried out deep in the bath and added after electrode heating, is easily mixed with the molten steel by contact with the molten steel, according to the gas imitation from the lance, and electrode heating for the purpose of melting is therefore not necessary. In addition, the flux (slag) that has been turned into a lotus in a short time continues to come into contact with the molten steel and mix vigorously, so that the slag-metal reaction progresses quickly and high refining performance is achieved. Fifth
Figure 5A is a sectional view showing an example of the steel taken to carry out the present invention, Figure 5B shows a heating mode using a heating electrode, and Figure 5B shows a refining mode using a lance. .

図示されるように、2は取鍋本体、2aは取鍋蓋、3は
溶鋼、4は加熱電極浸簿時のスラグ、4′は精錬用フラ
ックスを添加した後のスラグであり、取鍋蓋2aには、
取鍋内雰囲気調整用ガスの供給管5および取鍋内への添
加物のホッパ−6が取付けられており、さらに、取鍋蓋
2aには、昇降自在な加熱電極7およびガス吹込用のラ
ンス8が貫通している。9は取鋼本体2の上端と取鍋蓋
2aの下端との間に介在させた、耐熱性、気密性、およ
び可塑性に優れたシール材(たとえばカオール)である
As shown in the figure, 2 is the ladle body, 2a is the ladle lid, 3 is the molten steel, 4 is the slag when the heating electrode is immersed, 4' is the slag after adding the refining flux, and the ladle lid is In 2a,
A gas supply pipe 5 for adjusting the atmosphere inside the ladle and a hopper 6 for additives into the ladle are attached, and a heating electrode 7 that can be raised and lowered and a lance for blowing gas are attached to the ladle lid 2a. 8 is passing through. Reference numeral 9 denotes a sealing material (for example, Kaoru) having excellent heat resistance, airtightness, and plasticity, and is interposed between the upper end of the ladle main body 2 and the lower end of the ladle lid 2a.

なお図中矢印は、ランス8からのガス吹込による溶鋼3
の流れを示している。ついでこの発明の実施例について
説明する。漆鋼温度1640doで酸化精錬を終了した
25町on転炉からの漆鋼を、第5図イ,口に示す構造
の250Ton取鍋に出鋼(移注)した。次いで取鍋本
体に敬鍋蓋を装着し、メタケィ酸ソーダ5Tonを添加
し、T字2孔型のランスを溶鋼中に浸潰して2.0Nで
′minのArガスを溶鋼区に吹込開始し、同時に敬鍋
内に取鍋内雰囲気調整用ガスの供給管から空気を0.4
Nで/min供給開始して取鋼内を酸化性雰囲気にした
状態で、8分間精錬(ガス吹込)を行なった。ついで取
鍋スラグに加熱電極を浸潰し、通電を開始すると同時に
、ランスのガス吹込量を0.洲め′mjnに下げて18
分間溶鋼を鷹拝しながら加熱した。その結果、第1表に
示す通り、製鋼炉出鋼時に0/010%であった〔P〕
が、0.003%に低下した鋼が得られた。第1表 以上説明したように、この発明においては、きわめて、
Pの含有量の少ない鋼の得られる精錬方法を提供するこ
とができる。
Note that the arrow in the figure indicates molten steel 3 due to gas injection from lance 8.
It shows the flow. Next, embodiments of this invention will be described. The lacquered steel from the 25-town converter, which had undergone oxidation refining at a lacquered steel temperature of 1640 do, was tapped (transferred) into a 250-ton ladle having the structure shown in Fig. 5 (a) and (b). Next, a ladle lid was attached to the ladle body, 5 tons of sodium metasilicate was added, a T-shaped two-hole lance was immersed in the molten steel, and Ar gas of 2.0 N and 1 min was started to be blown into the molten steel. At the same time, 0.4 liters of air was introduced into the ladle from the gas supply pipe for adjusting the atmosphere inside the ladle.
Refining (gas injection) was performed for 8 minutes while supplying N at a rate of 1/min to create an oxidizing atmosphere inside the steel plate. Next, the heating electrode is immersed in the ladle slag, and at the same time as electricity is started, the amount of gas blown into the lance is reduced to 0. Down to 18
The molten steel was heated while stirring for a minute. As a result, as shown in Table 1, it was 0/010% [P] when steel was tapped in a steelmaking furnace.
However, a steel was obtained in which the content was reduced to 0.003%. As explained above in Table 1, in this invention, extremely
It is possible to provide a refining method that yields steel with a low P content.

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

第1図は製鋼炉(転炉)の耐火物熔損係数とその出鋼温
度との関係を示す図、第2図は製鋼炉(転炉)において
得られた素鋼の〔P〕とその出鋼温度との関係を示す図
、第3図はメタケィ酸ソーダを精錬用フラックスとして
用いたときの脱P率と溶鋼温度との関係を示す図、第4
図イ,口は、取鍋内溶鋼中に浸潰したランスの断面図、
第5図イ,口は、この発明を実施するための取鍋の一例
を示す断面図である。 1,1′,8・・・・・・ランス、2・・・・・・取鍋
本体、2a・・・・・・取鍋蓋、3・・・・・・溶鋼、
4,4′…・・・スラグ、5・・・・・・溶鋼内雰囲気
調整用ガスの供給管、6・…・・ホッパー、7・・…・
加熱電極、9……シール材。 菱l図 第3図 第2図 ※4図 第5図
Figure 1 shows the relationship between the refractory melting coefficient of a steelmaking furnace (converter) and its tapping temperature, and Figure 2 shows the [P] of raw steel obtained in a steelmaking furnace (converter) and its Figure 3 shows the relationship between the tapping temperature and the molten steel temperature.
Figure A: The mouth is a cross-sectional view of the lance immersed in the molten steel in the ladle.
FIG. 5A is a sectional view showing an example of a ladle for carrying out the present invention. 1, 1', 8... Lance, 2... Ladle body, 2a... Ladle lid, 3... Molten steel,
4,4'...Slag, 5...Gas supply pipe for adjusting the atmosphere inside molten steel, 6...Hopper, 7......
Heating electrode, 9...Sealing material. Diagram 3 Figure 2 *4 Figure 5

Claims (1)

【特許請求の範囲】[Claims] 1 製鋼炉で精錬された溶鋼を、密閉用蓋を有し、かつ
その内部にガスを吹込み可能にした取鍋に移注し、 つ
いで前記取鍋内溶鋼に精錬用フラツクスを添加し、 つ
いで前記取鍋内溶鋼中にその上方から浸漬した撹拌用ガ
スを吹込むためのランスから、前記溶鋼中に撹拌用ガス
の吹込みを行なうことによつて酸化性ガス雰囲気下で、
前記取鍋内溶鋼および前記溶鋼と前記溶鋼上のスラグと
を撹拌し、 ついで前記取鍋内溶鋼上のスラグに、加熱
電極の先端部を浸漬して、前記取鍋内溶鋼を所定温度に
加熱することを特徴とする溶鋼の精錬方法。
1. Transfer the molten steel refined in the steelmaking furnace to a ladle that has a sealing lid and into which gas can be blown, then add refining flux to the molten steel in the ladle, and then In an oxidizing gas atmosphere by blowing stirring gas into the molten steel from a lance for blowing stirring gas immersed into the molten steel in the ladle from above,
Stir the molten steel in the ladle, the molten steel, and the slag on the molten steel, and then immerse the tip of a heating electrode in the slag on the molten steel in the ladle to heat the molten steel in the ladle to a predetermined temperature. A method for refining molten steel characterized by:
JP55048268A 1980-04-12 1980-04-12 Molten steel refining method Expired JPS6037847B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55048268A JPS6037847B2 (en) 1980-04-12 1980-04-12 Molten steel refining method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55048268A JPS6037847B2 (en) 1980-04-12 1980-04-12 Molten steel refining method

Publications (2)

Publication Number Publication Date
JPS56146814A JPS56146814A (en) 1981-11-14
JPS6037847B2 true JPS6037847B2 (en) 1985-08-28

Family

ID=12798685

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JP55048268A Expired JPS6037847B2 (en) 1980-04-12 1980-04-12 Molten steel refining method

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JPS5223968A (en) * 1975-08-18 1977-02-23 Seiko Instr & Electronics Ltd Digital alarm watch

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JPS56146814A (en) 1981-11-14

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