JPS58221219A - Dephosphorization method of molten steel - Google Patents
Dephosphorization method of molten steelInfo
- Publication number
- JPS58221219A JPS58221219A JP10396482A JP10396482A JPS58221219A JP S58221219 A JPS58221219 A JP S58221219A JP 10396482 A JP10396482 A JP 10396482A JP 10396482 A JP10396482 A JP 10396482A JP S58221219 A JPS58221219 A JP S58221219A
- Authority
- JP
- Japan
- Prior art keywords
- molten steel
- steel
- slag
- ladle
- dephosphorization
- 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.)
- Granted
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)
- Manufacture And Refinement Of Metals (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は溶鋼の脱燐方法に関する。[Detailed description of the invention] The present invention relates to a method for dephosphorizing molten steel.
従来、溶鋼脱燐法として、CaO−FeO−Fe、0.
− CaF、 −5iO1−1110,系の7ラツクス
を、製鋼炉から取鍋へ出鋼する時の出鋼流へ添加する方
法や、Cab> 551 、 (FeO+Fe、O,)
> 2 F196 の7ラツクスを取鍋へ装入し、
その上に製鋼炉から溶鋼を出鋼して脱燐する方法等が知
られている。しかしながら、これらの方法は脱燐率が低
く、シかも溶鋼の温度低下が着しいため、コスト面や操
業面に問題があった。例えば上記フラックスを、出鋼時
に11〜12Kg/溶鋼TON添加しても、40〜50
%程度の脱燐率しか得られず、しかもそのときの溶鋼温
度は75〜95“0程度も低下する。また他の方法とし
て、N、、Co、を使用した脱燐法があるが、この方法
では上記した脱燐法に較べ脱燐率は良いが、溶鋼の温度
低下が通常の温度低下プラス50〜60°0と太きく、
シか4白煙が多量に発生するという難点がある。また、
以上の方法はいずれも大量の7ラツクスを用いなけれは
なら表いというコスト上の問題もある。Conventionally, as a molten steel dephosphorization method, CaO-FeO-Fe, 0.
- A method of adding 7 lux of CaF, -5iO1-1110, system to the tapping flow when steel is tapped from a steelmaking furnace to a ladle, or a method of adding CaF, -5iO1-1110, system 7 lux to the tapping stream when tapping steel from a steelmaking furnace to a ladle, or a method in which Cab > 551, (FeO + Fe, O,)
> 2 Charge 7 lux of F196 into the ladle,
In addition, a method is known in which molten steel is tapped from a steelmaking furnace and dephosphorized. However, these methods have low dephosphorization rates and cause problems in terms of cost and operation because the temperature of the molten steel is often lowered. For example, even if the above flux is added at 11 to 12 kg/ton of molten steel at the time of tapping, 40 to 50
%, and the molten steel temperature at that time drops by as much as 75-95%.Another method is the dephosphorization method using N, Co, etc. This method has a better dephosphorization rate than the above-mentioned dephosphorization method, but the temperature drop of the molten steel is as large as the normal temperature drop plus 50 to 60°0.
The problem is that a large amount of white smoke is generated. Also,
All of the above methods require the use of a large amount of 7 lux, which is a cost problem.
本発明はこのような事情に鑑み創案されたもので、上記
し九従来法のような問題を住せしめることなく、シかも
高価なフラックスを用いることなく高い効率で脱燐処理
を行うことができる方法を提供せんとするものである。The present invention was devised in view of these circumstances, and it is possible to perform dephosphorization treatment with high efficiency without having to suffer from the problems of the above-mentioned nine conventional methods and without using expensive flux. The purpose is to provide a method.
このため本発明は、製鋼炉で生成したスラグを、溶銅の
出鋼に際し溶鋼とともに取鍋内に排出し、スラグと溶鋼
を取鍋内で攪拌せしめることによシ脱燐兜理を行うよう
にした仁とをその基本的特徴とする。For this reason, the present invention provides a method for dephosphorizing slag produced in a steelmaking furnace by discharging it into a ladle together with molten steel when tapping molten copper, and stirring the slag and molten steel in the ladle. Its basic characteristic is the benevolence it possesses.
脱燐反応は溶鋼が低温はど促進されることが従来より知
られているが、一般に製鋼炉内吹止温度は出鋼時の温度
低下も考慮して1600°0以上にもな夛、この温度が
脱燐反応を阻害することに麦る。第1図はその一例を示
すもので、CaO451−8i0. ton−T、Fa
20%−Mg06q6を主成分としてMnO、A40
3 、 Ti01 。It has long been known that the dephosphorization reaction is accelerated when molten steel is heated to a low temperature, but the blow-off temperature in a steelmaking furnace is generally set at 1600° or higher, taking into account the temperature drop during tapping. Temperature may inhibit the dephosphorization reaction. FIG. 1 shows an example of this, with CaO451-8i0. ton-T, Fa
20%-MnO with Mg06q6 as the main component, A40
3, Ti01.
烏o、 、 s で構成されるスラグの脱燐能力と溶
鋼温度との関係を示している。このため製鋼炉中のスラ
グは未だ脱燐能力が十分あるにもかかわらず〔P〕を1
0多く含むことなく排出されてしまうのが通常である。It shows the relationship between the dephosphorization ability of slag composed of 0, , and s and the temperature of molten steel. For this reason, even though the slag in the steelmaking furnace still has sufficient dephosphorizing ability, [P] is reduced to 1.
Normally, it is discharged without containing much 0.
一方、取鍋内の溶鋼温度は製鋼炉内の温度よシも常に低
く、その差は50〜100°0にもなる。本発明者尋は
、上記したような製鋼炉から排出されたスラグの保有す
る脱燐能力と、製鋼炉内温度よ)も低い取鍋内溶鋼温度
に看目し、取鍋内の溶鋼温度によリスラグの脱燐能力を
活性化させることができ、従って取鍋内に溶鋼とともに
製鋼炉生成スラグを流出させ、これらを攪拌することに
より、効率的な脱燐処理を行い得ることを知見し九もの
である。On the other hand, the temperature of molten steel in the ladle is always lower than the temperature in the steelmaking furnace, and the difference therebetween is as much as 50 to 100 degrees. The present inventor, Hiro, took note of the dephosphorization ability of the slag discharged from the steelmaking furnace as described above, and the molten steel temperature in the ladle, which is lower than the temperature inside the steelmaking furnace. It was discovered that the dephosphorization ability of lithium slag can be activated, and that by flowing out the slag produced in a steelmaking furnace together with molten steel into the ladle and stirring them, efficient dephosphorization can be carried out. It is something.
また、製鋼炉生成スラグは、多量0*mポテンシャルを
有する友め、酸化鉄等の脱燐反応に必要なIII源を供
給する必要もない。In addition, the steelmaking furnace produced slag does not need to supply a large amount of metals having a 0*m potential, such as iron oxide, as a III source necessary for the dephosphorization reaction.
取鍋内における脱燐処理は、製鋼炉生成スラグと溶銅と
を攪拌することにより行うものであり、このため例えば
、取鍋内に攪拌ガス(例えばArガス)を供給しつつ攪
拌が行われる。The dephosphorization process in the ladle is performed by stirring the steelmaking furnace produced slag and molten copper, and for this reason, for example, stirring is performed while supplying a stirring gas (for example, Ar gas) into the ladle. .
250 TON転炉によ、9,1680”0で吹錬を終
了した溶銅を取鍋内に出鋼するとともに、転炉スラグも
取鍋内に流出させ、その後ガス流−Jio、 5 Nm
’/min (Arガス)によってスラグと溶f14を
20分間攪拌するという方法により、取鍋内への転炉ス
ラグの流出量を溶鋼TON当シ2.5時から60時まで
変化させ、攪拌後Om燐率を調べた。なお、取鍋内の溶
鋼温度は攪拌前で1610 ’0、攪拌後で1580℃
であシ、また処理前の溶鋼中CP)濃度は0.007〜
0.020優であった。その結果を第2図に示すが、こ
れによれば、取鍋内で脱燐反応が活性化され、効果的な
脱燐処理がなされておシ、特にスラグが溶鋼TON描シ
20即以上の場合60%以上の高い脱燐率が得られてい
ることが判る。Using the 250 TON converter, the molten copper that had been blown at a temperature of 9,1680"0 was tapped into the ladle, and the converter slag was also discharged into the ladle, followed by a gas flow of -Jio, 5 Nm.
By stirring the slag and molten f14 for 20 minutes using Ar gas/min (Ar gas), the flow rate of converter slag into the ladle was varied from 2.5 to 60 o'clock per molten steel TON, and after stirring, The Om phosphorus rate was investigated. The temperature of the molten steel in the ladle is 1610'0 before stirring and 1580°C after stirring.
In addition, the CP) concentration in molten steel before treatment is 0.007~
It was 0.020 well. The results are shown in Fig. 2, which shows that the dephosphorization reaction was activated in the ladle, and effective dephosphorization was carried out.In particular, the slag was more than 20 times larger than the molten steel TON. It can be seen that a high dephosphorization rate of 60% or more was obtained in this case.
以上述べた本発明によれば、従来法の如き太き表温度低
下や白煙の発生尋という問題を生ずることなく、シかも
フラックスを用いることなく効率的に脱燐処理を行うこ
とができるという優れた効果がある。According to the present invention as described above, dephosphorization can be carried out efficiently without the problems of conventional methods such as a large drop in surface temperature or generation of white smoke, and without using any flux. It has excellent effects.
第1図はスラグの脱燐能力と溶銅温度との関係を示した
ものである。第2図は本発明の実施例における転炉スラ
グ流出量と脱燐率との関係を示したものである。
特詐出願人 日本鋼管株式会社
第1図
1600 1640 1680 1720 17
60吹きiの滉& (’c)
第2図
10 2030 4050 60FIG. 1 shows the relationship between the slag dephosphorization ability and the molten copper temperature. FIG. 2 shows the relationship between the outflow amount of converter slag and the dephosphorization rate in an example of the present invention. Special fraud applicant Nippon Kokan Co., Ltd. Figure 1 1600 1640 1680 1720 17
60 blowing i's deep &('c) Fig. 2 10 2030 4050 60
Claims (1)
成したスラグも取鍋内に排出し、その後スラグと溶鋼を
取鍋内で攪拌せしめることを特徴とする溶鋼脱燐法。A molten steel dephosphorization method characterized by discharging slag generated in the steelmaking furnace into the ladle when tapping molten steel into the ladle (steelmaking furnace), and then stirring the slag and molten steel in the ladle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10396482A JPS58221219A (en) | 1982-06-18 | 1982-06-18 | Dephosphorization method of molten steel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10396482A JPS58221219A (en) | 1982-06-18 | 1982-06-18 | Dephosphorization method of molten steel |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58221219A true JPS58221219A (en) | 1983-12-22 |
JPS626607B2 JPS626607B2 (en) | 1987-02-12 |
Family
ID=14368048
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10396482A Granted JPS58221219A (en) | 1982-06-18 | 1982-06-18 | Dephosphorization method of molten steel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58221219A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0431455Y2 (en) * | 1987-12-29 | 1992-07-29 | ||
JPH0436516U (en) * | 1990-07-17 | 1992-03-26 | ||
JPH07286735A (en) * | 1994-04-15 | 1995-10-31 | Nippon Foil Mfg Co Ltd | Oil scatter preventive plate for gas range |
-
1982
- 1982-06-18 JP JP10396482A patent/JPS58221219A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS626607B2 (en) | 1987-02-12 |
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