JP3238016B2 - Hot metal pretreatment method - Google Patents
Hot metal pretreatment methodInfo
- Publication number
- JP3238016B2 JP3238016B2 JP21325394A JP21325394A JP3238016B2 JP 3238016 B2 JP3238016 B2 JP 3238016B2 JP 21325394 A JP21325394 A JP 21325394A JP 21325394 A JP21325394 A JP 21325394A JP 3238016 B2 JP3238016 B2 JP 3238016B2
- Authority
- JP
- Japan
- Prior art keywords
- lance
- hot metal
- reaction
- diameter
- immersion
- 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 - Fee Related
Links
Landscapes
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、下部が開放されており
上部から排気される容器である浸漬フリーボードの下部
を溶銑鍋に浸漬し、浸漬フリーボードの中央部よりラン
スを挿入して、溶銑の脱P処理を行うに際し、脱P反応
効率は従来レベルを維持しつつ、脱P処理中に浸漬フリ
ーボードおよび溶銑鍋の間に堆積したスラグのオーバー
フローを防止することを特徴とした溶銑の予備処理方法
に関するものである。BACKGROUND OF THE INVENTION The present invention has an open bottom part.
When immersing the lower part of the immersion free board, which is a container evacuated from the upper part, into a hot metal pot and inserting a lance from the center of the immersion free board to perform hot metal de-P treatment, the de-P reaction efficiency is lower than the conventional level. The present invention relates to a pretreatment method for hot metal characterized by preventing overflow of slag accumulated between a immersion free board and a hot metal pot during the de-P treatment while maintaining the same.
【0002】[0002]
【従来の技術】ランスより処理材を吹き込んで溶銑を処
理する場合、反応領域はその反応形態からランスの吐出
ノズル近傍の反応領域、スラグ−メタル界面反応領域
と、前記ランスの吐出ノズル近傍の反応領域から離脱し
横方向に広がりつつ浮上してスラグ−メタル界面反応領
域に至る間のトランジトリー反応領域に分けられる。従
来の技術は、脱P処理のトランジトリー反応のみに着目
し、下部槽の内径はランスより吐出した酸素および処理
材のジェットの広がりによる、トランジトリー反応を考
慮した横方向の最大到達距離に、ランスの径を加えて求
められた径より、500mm程度大きくした浸漬フリー
ボード下部槽が採用されていた。従って処理槽の作成の
簡便性、槽同志の脱着の容易性等から中間槽も下部槽と
ほぼ同一内径の構造をもって構成されていた。2. Description of the Related Art Hot metal is processed by blowing a processing material from a lance.
The lance discharge from the reaction mode
Reaction zone near nozzle, slag-metal interface reaction zone
From the reaction area near the discharge nozzle of the lance.
Slag-metal interface reaction area
The region is divided into a transient reaction region. The conventional technology focuses only on the transit reaction of the de-P treatment, and the inner diameter of the lower tank is the maximum reachable distance in the horizontal direction considering the transit reaction due to the spread of the jet of oxygen and the processing material discharged from the lance, An immersion freeboard lower tank that is larger by about 500 mm than the diameter obtained by adding the diameter of the lance has been employed. Therefore, the intermediate tank has a structure having substantially the same inner diameter as the lower tank because of the simplicity of preparation of the processing tank and the ease of detaching and attaching the tanks.
【0003】[0003]
【発明が解決しようとする課題】前記した従来技術は、
次の課題を有する。溶銑鍋と浸漬フリーボード下部外径
の間の容積が小さくなるために、脱P処理中の溶銑鍋と
浸漬フリーボード下部の間に堆積した脱Pスラグが、溶
銑鍋からオーバーフローするため、脱Pスラグに起因す
る処理設備トラブル、脱Pスラグオーバーフローを避け
るための送酸速度低下、更には、オーバーフローした脱
Pスラグの清掃頻度の増大という問題が発生し、生産性
が落ちていた。SUMMARY OF THE INVENTION
It has the following issues. Since the volume between the hot metal pot and the lower part of the immersion free board becomes smaller, the de-P slag accumulated between the hot metal pot and the lower part of the immersion free board during the de-P treatment overflows from the hot metal pot, so Problems such as processing equipment trouble due to slag, reduction in acid feed rate for avoiding overflow of de-P slag, and increase in frequency of cleaning of overflowed de-P slag occurred, resulting in reduced productivity.
【0004】[0004]
【課題を解決するための手段】本発明は、上記課題を解
決するためになされたものであり、その要旨とするとこ
ろは、溶銑鍋内の溶銑中に上部槽、中間槽、下部槽から
なる浸漬フリーボードの下部を浸漬し、その浸漬フリー
ボードの中央部よりランスを溶銑浴中に挿入し、酸素お
よび処理材を注入して溶銑の脱P処理を行うに際し、浸
漬フリーボードの中間槽内径は、ランスの吐出ノズル近
傍の反応領域からスラグ−メタル界面反応領域に至る間
の反応であるトランジトリー反応におけるランスより吐
出した酸素および処理材のジェットの広がりを考慮し
て、横方向の最大到達距離にランスの径を加えて求めら
れた径より大きくし、下部槽の内径は、ランスより吐出
した酸素および処理材のジェットの広がりによるトラン
ジトリー反応を考慮した、横方向の最大到達距離にラン
スの径を加えて求められた径とした、浸漬フリーボード
を用いることを特徴とする溶銑予備処理方法にある。SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and its gist is to form an upper tank, an intermediate tank, and a lower tank in hot metal in a hot metal pot. Immerse the lower part of the immersion freeboard, insert a lance into the hot metal bath from the center of the immersion freeboard, and inject oxygen and treatment material to remove the hot metal from the intermediate bath. Near the lance discharge nozzle
From the reaction zone at the side to the reaction zone at the slag-metal interface
In consideration of the spread of the oxygen discharged from the lance and the jet of the processing material in the transit reaction, which is the reaction of the above, the diameter obtained by adding the diameter of the lance to the maximum reach in the lateral direction is made larger than the diameter obtained by the inner diameter of the lower tank. Is characterized by the use of an immersion-free board, which is obtained by adding the diameter of the lance to the maximum reach in the horizontal direction, taking into account the transit reaction due to the spread of the oxygen discharged from the lance and the jet of the processing material. Hot metal pretreatment method.
【0005】[0005]
【作用】図3は溶銑鍋2内に浸漬フリーボード(上部槽
7a、中間槽7b、下部槽7c)を浸漬させた溶銑処理
を説明する模式図である。図中1は溶銑、3はランス、
4は吐出ノズル、5は処理材(ガス体と粉体の混合
物)、6はスラグである。図2は吐出ノズル口径27m
mで4個の吐出ノズルを有するランスより、酸素を流量
3600Nm3 /hrで供給したときの、処理材吹込み
ランスより吐出された粉体とガス体の広がり状況を示し
たものである。なお粉体は外管よりCaOとダスト、C
aF2 を900kg/minの速度で窒素ガスを搬送体
として吹込んだ。吐出粉体はランス吐出口より60cm
位離れた位置から上方に広がり始め、ほぼ95cm位で
その広がりは収束されている。このことにより下部槽7
cの内径は溶銑鍋2と浸漬フリーボード下部外径の間の
容積を可能な限り大きく保つため粉体最大広がり位置と
ほぼ等しい値を有する径が好ましい。一方、中間槽7b
においては、処理材の反応面を考慮し、反応界面が広い
方が反応にとって有利に作用するので、できるだけその
内径は広い方がよい。このような観点から溶銑鍋内で許
容できる範囲内で中間槽内径を大きくする方が好まし
い。FIG . 3 shows a freeboard (upper tank) immersed in a hot metal ladle 2.
7a, intermediate tank 7b, lower tank 7c)
FIG. In the figure, 1 is hot metal, 3 is lance,
4 is a discharge nozzle, 5 is a processing material (mixing of gas and powder)
Object) and 6 are slag. FIG. 2 shows a discharge nozzle diameter of 27 m.
This figure shows the spread state of the powder and gas discharged from the treatment material blowing lance when oxygen is supplied at a flow rate of 3600 Nm 3 / hr from a lance having four discharge nozzles at m. The powder is CaO and dust, C
It blows you a nitrogen gas as a carrier at a rate of aF 2 900kg / min. Discharge powder is 60cm from lance discharge port
It begins to spread upward from a position farther away, and the spread is converged at about 95 cm. This allows the lower tank 7
The inner diameter of c is preferably a diameter having a value substantially equal to the maximum spread position of the powder in order to keep the volume between the hot metal pot 2 and the outer diameter of the lower part of the immersion free board as large as possible. On the other hand, the intermediate tank 7b
In the above, considering the reaction surface of the treatment material, a wider reaction interface is more advantageous for the reaction, so the inner diameter is preferably as large as possible. From such a viewpoint, it is preferable to increase the inner diameter of the intermediate tank within an allowable range in the hot metal pot.
【0006】本発明はかかる知見に基づいてなされたも
のであって、溶銑鍋2内の溶銑中に上部槽7a、中間槽
7b、下部槽7cからなる浸漬フリーボードの下部を浸
漬し、その浸漬フリーボードの中央部よりランス3を溶
銑浴中に挿入し、酸素および処理材を注入して溶銑のP
処理を行う場合の浸漬フリーボードの径を定めるにあた
り、トップスラグ−メタル間のパーマネント反応に影響
をあたえる中間槽7bの内径は、ランスより吐出した酸
素および処理材のジェットの広がりによるトランジトリ
ー反応を考慮した、横方向の最大到達距離にランスの径
を加えて求められた径より大きくし、下部槽7c内径
は、ランス3より吐出した酸素および処理材のジェット
の広がりによるトランジトリー反応を考慮した、横方向
の最大到達距離にランスの径A(図3)を加えて求めら
れた径としたものである。The present invention was made on the basis of this finding, the upper tank 7a, the intermediate tank during the hot metal in the hot metal pot in 2
7b , the lower part of the immersion freeboard consisting of the lower tank 7c is immersed, the lance 3 is inserted into the hot metal bath from the center of the immersion freeboard, oxygen and the processing material are injected, and P
In determining the diameter of the immersion free board when performing the treatment, the inner diameter of the intermediate tank 7b which affects the permanent reaction between the top slag and the metal is determined by the transit reaction due to the spread of the oxygen discharged from the lance and the jet of the treatment material. The diameter obtained by adding the diameter of the lance to the maximum lateral distance considered was made larger than the diameter obtained, and the inner diameter of the lower tank 7c took into account the transient reaction due to the spread of the oxygen discharged from the lance 3 and the jet of the processing material. , Obtained by adding the lance diameter A (FIG. 3) to the maximum lateral distance.
【0007】[0007]
【実施例】表1に実施例に用いた浸漬フリーボードの諸
元と従来例と共に示した。図1には脱P酸素効率を本発
明例と従来例を比較して示したが、本発明によるものは
平均値でみれば酸素効率が優れていることが判る。EXAMPLES Table 1 shows the specifications of the immersion free board used in the examples and the conventional examples. FIG. 1 shows the deoxidation efficiency of the present invention and the conventional example in comparison, and it can be seen that the oxygen efficiency of the present invention is excellent in terms of the average value.
【0008】[0008]
【表1】 [Table 1]
【0009】また、表1から明らかなように浸漬フリー
ボード下部槽と溶銑鍋内張りとの間隙が従来のものより
250mmも拡がり溶銑鍋内に堆積した脱Pスラグが鍋
からオーバーフローすることがなかった。Further, as is clear from Table 1, the gap between the lower tank of the immersion freeboard and the lining of the hot metal pot was expanded by 250 mm as compared with the conventional one, and the de-P slag deposited in the hot metal pot did not overflow from the pot. .
【0010】[0010]
【発明の効果】本発明により、脱P反応効率は従来レベ
ルを維持しつつ、脱P処理中のスラグのオーバーフロー
を防止することが可能となり、脱Pスラグによる設備ト
ラブル、送酸速度低下、更には脱Pスラグ清掃頻度を低
減し、生産性を向上させることが可能となった。According to the present invention, it is possible to prevent the slag from overflowing during the de-P treatment while maintaining the conventional de-P reaction efficiency at the conventional level. Has reduced the frequency of removing P-slag and has improved the productivity.
【図1】CaO/Oと脱P酸素効率の関係を示す図FIG. 1 is a diagram showing a relationship between CaO / O and deoxygenation efficiency.
【図2】ランスより吐出した粉体・ガスの軌跡を示す図FIG. 2 is a diagram showing a trajectory of powder and gas discharged from a lance.
【図3】溶銑鍋内に浸漬フリーボードを浸漬させた溶銑
処理を説明する模式図 Fig. 3 Hot metal immersed in immersion freeboard in hot metal ladle
Schematic diagram explaining processing
【符号の説明】1 溶銑 2 溶銑鍋 3 ランス 4 吐出ノズル 5 処理材 6 スラグ 7a 浸漬フリーボードの上部槽 7b 浸漬フリーボードの中間槽 7c 浸漬フリーボードの下部槽 [Description of Signs ] 1 hot metal 2 hot metal ladle 3 lance 4 discharge nozzle 5 treatment material 6 slag 7a upper tank of immersion free board 7b intermediate tank of immersion free board 7c lower tank of immersion free board
───────────────────────────────────────────────────── フロントページの続き (72)発明者 松尾 慎二 大分県大分市大字西ノ洲1番地 新日本 製鐵株式会社 大分製鐵所内 (72)発明者 寺西 精造 大分県大分市大字西ノ洲1番地 新日本 製鐵株式会社 大分製鐵所内 (58)調査した分野(Int.Cl.7,DB名) C21C 1/02 ──────────────────────────────────────────────────の Continuing on the front page (72) Inventor Shinji Matsuo Oita, Oita, Oita, 1st section, Nishinosu Oita Works Nippon Steel Corporation (72) Inventor Teranishi, Seiko 1st section, Oita, Oita, Oaza, 1F Steel Works Co., Ltd. Oita Works (58) Fields surveyed (Int. Cl. 7 , DB name) C21C 1/02
Claims (1)
部槽からなる浸漬フリーボードの下部を浸漬し、その浸
漬フリーボードの中央部よりランスを溶銑浴中に挿入
し、酸素および処理材を注入して溶銑の脱P処理を行う
に際し、浸漬フリーボードの中間槽内径は、ランスの吐
出ノズル近傍の反応領域からスラグ−メタル界面反応領
域に至る間の反応であるトランジトリー反応におけるラ
ンスより吐出した酸素および処理材のジェットの広がり
を考慮して、横方向の最大到達距離にランスの径を加え
て求められた径より大きくし、下部槽の内径は、ランス
より吐出した酸素および処理材のジェットの広がりによ
るトランジトリー反応を考慮した、横方向の最大到達距
離にランスの径を加えて求められた径とした、浸漬フリ
ーボードを用いることを特徴とする溶銑予備処理方法。1. A immersion freeboard comprising an upper tank, an intermediate tank, and a lower tank is immersed in hot metal in a hot metal ladle, and a lance is inserted into the hot metal bath from a central portion of the immersion freeboard. upon by injecting treatment material performs de-P treatment of molten pig iron, the intermediate tank inner diameter of the immersion freeboard is Reims ejection
Slag-metal interface reaction zone from the reaction zone near the discharge nozzle
It was calculated by adding the lance diameter to the maximum lateral distance, taking into account the oxygen discharged from the balance and the spread of the jet of the processing material in the transit reaction, which is the reaction during the reaction up to the zone . The inner diameter of the lower tank was determined by adding the diameter of the lance to the maximum lateral distance, taking into account the transit reaction due to the spread of the jet of oxygen and processing material discharged from the lance, and the diameter of the lance. And a hot metal pretreatment method characterized by using an immersion free board.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21325394A JP3238016B2 (en) | 1994-08-16 | 1994-08-16 | Hot metal pretreatment method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21325394A JP3238016B2 (en) | 1994-08-16 | 1994-08-16 | Hot metal pretreatment method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0860216A JPH0860216A (en) | 1996-03-05 |
JP3238016B2 true JP3238016B2 (en) | 2001-12-10 |
Family
ID=16636042
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21325394A Expired - Fee Related JP3238016B2 (en) | 1994-08-16 | 1994-08-16 | Hot metal pretreatment method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3238016B2 (en) |
-
1994
- 1994-08-16 JP JP21325394A patent/JP3238016B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0860216A (en) | 1996-03-05 |
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Legal Events
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A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20010911 |
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LAPS | Cancellation because of no payment of annual fees |