JPH0160526B2 - - Google Patents
Info
- Publication number
- JPH0160526B2 JPH0160526B2 JP12558183A JP12558183A JPH0160526B2 JP H0160526 B2 JPH0160526 B2 JP H0160526B2 JP 12558183 A JP12558183 A JP 12558183A JP 12558183 A JP12558183 A JP 12558183A JP H0160526 B2 JPH0160526 B2 JP H0160526B2
- Authority
- JP
- Japan
- Prior art keywords
- molten steel
- dephosphorization
- added
- molten
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/064—Dephosphorising; 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
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、
容器内に収容された、酸素濃度が400ppm以上
の未脱酸溶鋼中に、精錬炉で溶鉄の精錬に使用し
た酸化性の溶融スラグと、生石灰とを各々所定量
添加した上、前記溶鋼をアーク熱により加熱し、
且つ、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。
次いで、容器2内の溶鋼3中に、所定量の生石
灰と、転炉1において溶鉄の精錬に使用したまだ
脱燐能を有する、下記第1表に示す成分組成の所
定量の酸化性の溶融スラグ(以下、精錬炉スラグ
という)とを添加する。
次に、上記により生石灰および精錬炉スラグの
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. A predetermined amount of oxidizing molten slag used for refining molten iron in a smelting furnace and quicklime were added to undeoxidized molten steel with an oxygen concentration of 400 ppm or more, which was housed in a smelting furnace. heated by
Further, the present invention is characterized in that the molten steel is dephosphorized by forcibly stirring the molten steel. 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. Next, in the molten steel 3 in the container 2, a predetermined amount of quicklime and a predetermined amount of oxidizing molten metal having the composition shown in Table 1 below, which has been used for refining the molten iron in the converter 1 and still has dephosphorizing ability, are added. Slag (hereinafter referred to as smelting furnace slag) is added. Next, the quicklime and smelting furnace slag are
【表】
添加された溶鋼を、第1図Bに示すように、電極
4によるアーク熱によつて加熱し、且つ、ランス
5から噴射されるアルゴンガスのような不活性ガ
スにより攪拌する。その結果、容器2内に収容さ
れた溶鋼3中の脱燐スラグの滓化は促進され、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。
容器内に収容された燐含有量が5×10-3〜8×
10-3wt%の溶鋼に対し、16〜20Kg/Tの量の精
錬炉スラグと、4〜6Kg/Tの生石灰とを添加し
た。次いで前記精錬炉スラグおよび生石灰の添加
された溶鋼を、2000〜3000KWHの電力によるア
ーク熱によつて約10分間加熱し、且つ、2000/
mmの量のアルゴンガスの吹込みによつて約10分間
強制的に攪拌した。
第2図は、上記による処理後の燐含有量であ
る。第2図において、白丸印は上述した本発明方
法によつて脱燐した場合を示し、白三角印は比較
例として生石灰および精錬炉スラグの添加のみの
場合、黒三角印は同じく比較例として精錬炉スラ
グの添加のみの場合を各々示す。
第2図からわかるように、精錬炉スラグの添加
のみの場合の脱燐率は約35%、生石灰および精錬
炉スラグの添加のみの場合の脱燐率は約45%であ
るのに対し、この発明方法の場合の脱燐率は約65
%に向上した。
第2表は、精錬炉スラグおよび生石灰の添加
量、アーク熱による加熱時間および攪拌用ガス吹
込条件を変えた場合の脱燐率である。
第2図および第2表からわかるように、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55〜70%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[Table] As shown in FIG. 1B, the added molten steel is heated by arc heat from an electrode 4 and stirred by an inert gas such as argon gas injected from a lance 5. As a result, the dephosphorization slag in the molten steel 3 housed in the container 2 is promoted to become slag, 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. The phosphorus content contained in the container is 5×10 -3 to 8×
Refining furnace slag in an amount of 16 to 20 Kg/T and quicklime in an amount of 4 to 6 Kg/T were added to 10 -3 wt% of molten steel. Next, the molten steel to which the smelting furnace slag and quicklime have been added is heated for about 10 minutes by arc heat using an electric power of 2000 to 3000 KWH, and
Forced stirring was carried out for about 10 minutes by blowing in argon gas in an amount of mm. FIG. 2 shows the phosphorus content after the above treatment. In Figure 2, white circles indicate the case of dephosphorization using the above-mentioned method of the present invention, white triangles indicate the case of adding only quicklime and smelting furnace slag as a comparative example, and black triangles indicate the case of smelting as a comparative example. The cases in which only furnace slag is added are shown in each case. As can be seen from Figure 2, the dephosphorization rate when only adding smelter slag is about 35%, and when only quicklime and smelting furnace slag are added, the dephosphorization rate is about 45%. The dephosphorization rate for the invented method is approximately 65
%. Table 2 shows the dephosphorization rates when the amounts of smelter slag and quicklime added, the heating time using arc heat, and the stirring gas injection conditions were changed. As can be seen from FIG. 2 and Table 2, the dephosphorization rate of molten steel when dephosphorized by the method of this invention was 55 to 70%, and an excellent dephosphorization effect was obtained. As described above, according to the method of this invention, inexpensive quicklime is used as a dephosphorizing agent, and the quicklime is
【表】【table】
【表】
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] Efficient dephosphorization can be carried out by maximizing the dephosphorizing ability, and therefore, an excellent industrial effect is brought about in which ultra-low phosphorus steel of excellent quality can be manufactured at low cost. .
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…電極、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 FIG. 2 is a graph showing the dephosphorization rate when treated by the method of this invention. In the drawings: 1... Converter, 2... Container, 3... Molten steel, 4... Electrode, 5
...Lance, 6...Vacuum slag removal device.
Claims (1)
上の未脱酸溶鋼中に、精錬炉で溶鉄の精錬に使用
した酸化性の溶融スラグと、生石灰とを各々所定
量添加した上、前記溶鋼をアーク熱により加熱
し、且つ、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. To undeoxidized molten steel with an oxygen concentration of 400 ppm or more housed in a container, predetermined amounts of oxidizing molten slag used for refining molten iron in a smelting furnace and quicklime are added, and then the molten steel is A method for dephosphorizing molten steel, characterized in that the molten steel is dephosphorized by heating with arc heat and forcibly stirring the molten steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12558183A JPS6021317A (en) | 1983-07-12 | 1983-07-12 | Method for dephosphorizing molten steel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12558183A JPS6021317A (en) | 1983-07-12 | 1983-07-12 | Method for dephosphorizing molten steel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6021317A JPS6021317A (en) | 1985-02-02 |
| JPH0160526B2 true JPH0160526B2 (en) | 1989-12-22 |
Family
ID=14913720
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12558183A Granted JPS6021317A (en) | 1983-07-12 | 1983-07-12 | Method for dephosphorizing molten steel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6021317A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63203248A (en) * | 1987-02-18 | 1988-08-23 | Kawasaki Steel Corp | Melting method for bearing steel |
-
1983
- 1983-07-12 JP JP12558183A patent/JPS6021317A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6021317A (en) | 1985-02-02 |
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