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JPH0160525B2 - - Google Patents
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JPH0160525B2 - - Google Patents

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Publication number
JPH0160525B2
JPH0160525B2 JP12558083A JP12558083A JPH0160525B2 JP H0160525 B2 JPH0160525 B2 JP H0160525B2 JP 12558083 A JP12558083 A JP 12558083A JP 12558083 A JP12558083 A JP 12558083A JP H0160525 B2 JPH0160525 B2 JP H0160525B2
Authority
JP
Japan
Prior art keywords
molten steel
container
dephosphorization
slag
quicklime
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
JP12558083A
Other languages
Japanese (ja)
Other versions
JPS6021316A (en
Inventor
Hitoshi Kobayashi
Yoshimi Komatsu
Seishi Mizuoka
Osamu Yamase
Yasuhiro Matsuda
Tsutomu Usui
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 JP12558083A priority Critical patent/JPS6021316A/en
Publication of JPS6021316A publication Critical patent/JPS6021316A/en
Publication of JPH0160525B2 publication Critical patent/JPH0160525B2/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
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/04Removing impurities by adding a treating agent
    • C21C7/064Dephosphorising; Desulfurising

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Steel In Its Molten State (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は、溶鋼の脱燐方法に関するものであ
る。 鋼中の不純物元素である燐の除去方法として、
次のような方法が知られている。 溶銑の予備処理方法 転炉吹錬中における脱燐方法 転炉ダブルスラグ方法 容器内溶鋼の脱燐方法 しかしながら、上記の方法は処理コストが高
く、上記の方法は脱燐能に限界があり、上記
の方法は転炉々体に悪影響を及ぼし、そして、上
記の方法は添加する脱燐用フラツクスが高価な
ため処理コストが高くなる問題があつた。 近時、極低燐鋼の要求が強いが、燐含有量が
0.005wt%以下の極低燐鋼は、上記の方法では
製造不可能であり、また上記の方法では転炉々
体に及ぼす悪影響が大きい。そこで、このような
極低燐鋼は、通常上記またはの方法によつて
製造されているが、これらの方法では、上述した
ようにコスト高となる問題がある。 この発明は、上述のような観点から、低コスト
で脱燐処理を行なうことができ、品質の優れた極
低燐鋼を効率的に製造し得る溶鋼の脱燐方法を提
供するもので、 精錬炉で溶製された、酸素濃度が400ppm以上
の未脱酸溶鋼を、前記精錬炉から容器内に流下さ
せて前記容器内に供給し、前記溶鋼が流下中の前
記容器内に所定量の生石灰を投入し、且つ、前記
容器内の溶鋼中に、前記精錬炉で溶鉄の精錬に使
用した所定量の酸化性の溶融スラグを添加し、そ
して、前記容器内の前記溶鋼を強制的に攪拌する
ことにより前記溶鋼の脱燐を行なうことに特徴を
有するものである。 次に、この発明を図面を参照して説明する。 第1図はこの発明方法の一実施態様を示す工程
図である。第1図において、1は酸化精錬炉の一
例としての転炉、2は容器で、同図Aに示すよう
に、転炉1により精錬された、鋼中の酸素濃度が
400ppm以上の未脱酸溶鋼3を、転炉1から出鋼
し、容器2内に収容する。このとき、転炉1から
溶鋼3が流下中の容器2内に、溶鋼3の落下点を
目ざしてシユート4から所定量の生石灰(CaO)
を投入する。 そして、転炉1において溶鉄の精錬に使用した
まで脱燐能を有する、下記第1表に示す成分組成
の酸化性の溶融スラグ(以下、精錬炉スラグとい
う)の所定量を、転炉1から容器2内の溶鋼中に
添加する。
The present invention relates to a method for dephosphorizing molten steel. As a method for removing phosphorus, an impurity element in steel,
The following methods are known. Preliminary treatment method for hot metal Dephosphorization method during converter blowing Converter double slag method Dephosphorization method for molten steel in a vessel However, the above methods have high processing costs, and the above methods have limited dephosphorization ability. The above method had a negative effect on the converter body, and the above method had the problem of increasing processing costs because the dephosphorization flux added was expensive. Recently, there has been a strong demand for ultra-low phosphorus steel, but
Ultra-low phosphorus steel of 0.005wt% or less cannot be produced by the above method, and the above method has a large negative effect on the converter body. Therefore, such ultra-low phosphorus steel is usually manufactured by the above-mentioned method, but these methods have the problem of high cost as described above. From the above-mentioned viewpoints, the present invention provides a method for dephosphorizing molten steel that can perform dephosphorization treatment at low cost and efficiently produce ultra-low phosphorus steel of excellent quality. Undeoxidized molten steel melted in a furnace and having an oxygen concentration of 400 ppm or more is allowed to flow down from the refining furnace into a container, and a predetermined amount of quicklime is poured into the container while the molten steel is flowing down. and adding a predetermined amount of oxidizing molten slag used for refining molten iron in the refining furnace to the molten steel in the container, and forcibly stirring the molten steel in the container. This method is characterized in that the molten steel is dephosphorized by this method. Next, the present invention will be explained with reference to the drawings. FIG. 1 is a process diagram showing one embodiment of the method of this invention. In Figure 1, 1 is a converter as an example of an oxidation refining furnace, 2 is a container, and as shown in Figure A, the oxygen concentration in the steel refined by the converter 1 is
Undeoxidized molten steel 3 having a concentration of 400 ppm or more is tapped from a converter 1 and stored in a container 2. At this time, a predetermined amount of quicklime (CaO) is poured from the chute 4 into the container 2 where the molten steel 3 is flowing down from the converter 1, aiming at the falling point of the molten steel 3.
Insert. Then, a predetermined amount of oxidizing molten slag (hereinafter referred to as smelting furnace slag) having the composition shown in Table 1 below, which has a dephosphorizing ability until used for refining molten iron in the converter 1, is transferred from the converter 1. It is added to the molten steel in the container 2.

【表】 生石灰(CaO)は、上述したように、容器2内
に転炉1から溶鋼3が流下している状態のとき
に、容器2内の溶鋼中に投入することが必要であ
る。即ち、投入された生石灰は、容器2内におけ
る溶鋼3の落下流により生ずる攪拌力で十分に滓
化され、その結果溶鋼の脱燐は効率的に行なわれ
る。なお予め生石灰が装入された容器内に受鋼す
る方法では、生石灰は十分に滓化せず、溶鋼の脱
燐率も低い。 このようにして、容器2内の溶鋼3中に添加さ
れた生石灰および精錬炉スラグにより、溶鋼3の
脱燐は進行し、前記生石灰と精錬炉スラグとによ
る脱燐スラグが生成する。 次に、上記により生石灰および精錬炉スラグの
添加された溶鋼3中に、第1図Bに示すようにラ
ンス5から例えばアルゴンガスのような不活性ガ
スを噴射し、前記ガスにより溶鋼3を強制的に攪
拌する。このような溶鋼3の強制攪拌によつて、
脱燐スラグの滓化が促進され、溶鋼3は効率的に
脱燐される。 次いで、脱燐処理の終了した溶鋼の湯面上にあ
る溶鋼脱燐後のスラグを、第1図Cに示すように
真空除滓装置6により吸収して除去し、前記スラ
グによる鋼中への復燐を防止する。 この発明において、脱燐処理を施す溶鋼は、鋼
中の酸素濃度が400ppm以上の未脱酸溶鋼である
ことを必要とする。即ち鋼中の酸素濃度が
400ppm未満では、活発な脱燐反応を起させるこ
とができない。 溶鋼中に添加する精錬炉スラグの量は、溶鋼1
屯当り15〜30Kgが好ましい。即ち、精錬炉スラグ
の添加量が15Kg/T未満では脱燐作用が不十分で
あり、一方、30Kg/Tを超えると溶鋼の攪拌時に
取鍋から溶融スラグが溢出する問題が生ずる。 また、前記溶鋼中に添加する生石灰(CaO)の
量は、溶鋼1屯当り2〜10Kgが好ましい。即ち、
前記生石灰の添加量が2Kg/T未満では脱燐作用
が不十分であり、一方、10Kg/Tを超えると溶鋼
が冷却して凝固するおそれが生ずる。 次に、この発明を実施例によつて説明する。 250T転炉において精錬した、P含有量0.010〜
0.020wt%、酸素濃度500〜700ppmで、1670℃の
温度の溶鋼を、前記転炉から容器内に供給した。
そして、容器内の溶鋼中に15Kg/Tおよび20Kg/
Tの転炉スラグを添加し、且つ、前記溶鋼が流下
中の容器内に、2〜6Kg/Tの生石灰(CaO)を
投入した。 次いで、容器内の溶鋼中に、2000/mmの量の
アルゴンガスを吹込んで前記溶鋼を強制的に攪拌
し、脱燐処理を行なつた後、真空除滓装置で除滓
した。脱燐後の溶鋼温度は1580℃であつた。 第2図は15Kg/Tの転炉スラグを添加した場合
の脱燐率、第3図は20Kg/Tの転炉スラグを添加
した場合の脱燐率である。第2図および第3図に
おいて、白丸印は本発明方法により溶鋼が流下中
の容器内に生石灰を投入した場合、黒丸印は予め
容器内に生石灰を装入した場合の脱燐率を示す。 第2図および第3図からわかるように、この発
明方法によつて脱燐処理を行なつた場合の溶鋼の
脱燐率は60〜65%であり、優れた脱燐効果が得ら
れた。 以上述べたように、この発明方法によれば、脱
燐剤として安価な生石灰を使用し、前記生石灰の
脱燐能を最大限に発揮せしめて効率的な脱燐処理
を行なうことができ、従つて品質の優れた極低燐
鋼を低コストで製造し得る工業上優れた効果がも
たらされる。
[Table] As mentioned above, quicklime (CaO) needs to be added to the molten steel in the container 2 when the molten steel 3 is flowing down from the converter 1 into the container 2. That is, the charged quicklime is sufficiently turned into slag by the stirring force generated by the falling flow of the molten steel 3 in the container 2, and as a result, the molten steel is efficiently dephosphorized. In addition, in the method of receiving steel in a container in which quicklime is charged in advance, the quicklime is not sufficiently turned into slag, and the dephosphorization rate of molten steel is low. In this way, dephosphorization of the molten steel 3 progresses due to the quicklime and smelting furnace slag added to the molten steel 3 in the container 2, and dephosphorization slag is produced by the quicklime and smelting furnace slag. Next, as shown in FIG. 1B, an inert gas such as argon gas is injected from a lance 5 into the molten steel 3 to which quicklime and smelting furnace slag have been added, and the molten steel 3 is forced by the gas. Stir thoroughly. By such forced stirring of the molten steel 3,
The slag formation of the dephosphorization slag is promoted, and the molten steel 3 is efficiently dephosphorized. Next, the slag after dephosphorization of the molten steel on the surface of the molten steel after the dephosphorization process is absorbed and removed by the vacuum slag removal device 6 as shown in FIG. Prevents rephosphorization. In this invention, the molten steel to be dephosphorized needs to be undeoxidized molten steel with an oxygen concentration of 400 ppm or more. In other words, the oxygen concentration in the steel is
At less than 400 ppm, active dephosphorization reaction cannot occur. The amount of refining furnace slag added to molten steel is
15 to 30 kg per tonne is preferred. That is, if the amount of smelting furnace slag added is less than 15 kg/T, the dephosphorization effect is insufficient, while if it exceeds 30 kg/T, a problem arises in which molten slag overflows from the ladle when stirring the molten steel. Further, the amount of quicklime (CaO) added to the molten steel is preferably 2 to 10 kg per ton of molten steel. That is,
If the amount of added quicklime is less than 2 kg/T, the dephosphorization effect will be insufficient, while if it exceeds 10 kg/T, there is a risk that the molten steel will cool and solidify. Next, the present invention will be explained with reference to examples. Refined in a 250T converter, P content 0.010~
Molten steel of 0.020 wt%, oxygen concentration of 500 to 700 ppm, and a temperature of 1670°C was supplied from the converter into the vessel.
Then, 15Kg/T and 20Kg/T were added to the molten steel in the container.
T of converter slag was added, and 2 to 6 kg/T of quicklime (CaO) was charged into the container in which the molten steel was flowing down. Next, 2000/mm of argon gas was blown into the molten steel in the container to forcibly stir the molten steel to perform a dephosphorization treatment, and then the slag was removed using a vacuum slag removal device. The temperature of the molten steel after dephosphorization was 1580°C. Figure 2 shows the dephosphorization rate when 15 kg/T of converter slag is added, and Figure 3 shows the dephosphorization rate when 20 kg/T of converter slag is added. In FIGS. 2 and 3, white circles indicate the dephosphorization rate when quicklime is charged into a container in which molten steel is flowing according to the method of the present invention, and black circles indicate the dephosphorization rate when quicklime is charged into the container in advance. As can be seen from FIGS. 2 and 3, the dephosphorization rate of molten steel when dephosphorized by the method of this invention was 60 to 65%, and an excellent dephosphorization effect was obtained. As described above, according to the method of the present invention, it is possible to use inexpensive quicklime as a dephosphorizing agent, maximize the dephosphorizing ability of the quicklime, and perform efficient dephosphorization treatment. As a result, an excellent industrial effect is produced in which ultra-low phosphorus steel of excellent quality can be manufactured at low cost.

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

第1図はこの発明方法の一実施態様を示す工程
図、第2図および第3図はこの発明方法によつて
処理した場合の脱燐率を示すグラフである。図面
において、1…転炉、2…容器、3…溶鋼、4…
シユート、5…ランス、6…真空除滓装置。
FIG. 1 is a process diagram showing one embodiment of the method of this invention, and FIGS. 2 and 3 are graphs showing the dephosphorization rate when treated by the method of this invention. In the drawings, 1... converter, 2... container, 3... molten steel, 4...
Chute, 5... Lance, 6... Vacuum slag removal device.

Claims (1)

【特許請求の範囲】[Claims] 1 精錬炉で溶製された、酸素濃度が400ppm以
上の未脱酸溶鋼を、前記精錬炉から容器内に流下
させて前記容器内に供給し、前記溶鋼が流下中の
前記容器内に所定量の生石灰を投入し、且つ、前
記容器内の溶鋼中に、前記精錬炉で溶鉄の精錬に
使用した所定量の酸化性の溶融スラグを添加し、
そして、前記容器内の前記溶鋼を強制的に攪拌す
ることにより前記溶鋼の脱燐を行なうことを特徴
とする溶鋼の脱燐方法。
1. Undeoxidized molten steel melted in a refining furnace and having an oxygen concentration of 400 ppm or more is supplied into the container by flowing down from the refining furnace into the container, and a predetermined amount of the molten steel is poured into the container while it is flowing down. of quicklime, and adding a predetermined amount of oxidizing molten slag used for refining molten iron in the refining furnace to the molten steel in the container,
A method for dephosphorizing molten steel, characterized in that the molten steel in the container is dephosphorized by forcibly stirring the molten steel.
JP12558083A 1983-07-12 1983-07-12 Method for dephosphorizing molten steel Granted JPS6021316A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12558083A JPS6021316A (en) 1983-07-12 1983-07-12 Method for dephosphorizing molten steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12558083A JPS6021316A (en) 1983-07-12 1983-07-12 Method for dephosphorizing molten steel

Publications (2)

Publication Number Publication Date
JPS6021316A JPS6021316A (en) 1985-02-02
JPH0160525B2 true JPH0160525B2 (en) 1989-12-22

Family

ID=14913697

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12558083A Granted JPS6021316A (en) 1983-07-12 1983-07-12 Method for dephosphorizing molten steel

Country Status (1)

Country Link
JP (1) JPS6021316A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62205221A (en) * 1986-03-04 1987-09-09 Nippon Steel Corp Method for degassing and dephosphorizing molten steel

Also Published As

Publication number Publication date
JPS6021316A (en) 1985-02-02

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