JP2812852B2 - Hot metal desiliconization and dephosphorization method - Google Patents

Hot metal desiliconization and dephosphorization method

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Publication number
JP2812852B2
JP2812852B2 JP5068313A JP6831393A JP2812852B2 JP 2812852 B2 JP2812852 B2 JP 2812852B2 JP 5068313 A JP5068313 A JP 5068313A JP 6831393 A JP6831393 A JP 6831393A JP 2812852 B2 JP2812852 B2 JP 2812852B2
Authority
JP
Japan
Prior art keywords
lance
hot metal
powder
pipe
oxygen
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
Application number
JP5068313A
Other languages
Japanese (ja)
Other versions
JPH06279825A (en
Inventor
健史 鈴木
參 中戸
光紀 牧野
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 Steel Corp
Original Assignee
JFE Steel Corp
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 JFE Steel Corp filed Critical JFE Steel Corp
Priority to JP5068313A priority Critical patent/JP2812852B2/en
Publication of JPH06279825A publication Critical patent/JPH06279825A/en
Application granted granted Critical
Publication of JP2812852B2 publication Critical patent/JP2812852B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
  • Furnace Charging Or Discharging (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、溶銑の脱珪、脱燐方法
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for desiliconizing and dephosphorizing hot metal.

【0002】[0002]

【従来の技術】現在では転炉装入前の溶銑に対して予備
脱珪、脱燐および脱硫を施し、転炉では脱炭のみを行う
ことによって精錬工程のトータルコストを低減するプロ
セスが広く普及している。溶銑の予備脱珪、脱燐に際し
ては、トピードカーまたは溶銑鍋に充填した溶銑中に、
ランスを浸漬して酸化鉄を主成分とする固体酸化物(以
下固体酸素と称する)および生石灰等の脱燐剤を消耗式
の浸漬ランスを介して吹き込む方法が多く採用されてき
た。このプロセスの最大の弱点は固体酸素の分解熱およ
び固体酸素や生石灰等の顕熱増により溶銑温度が大幅に
低下し、次工程である転炉での熱余裕度が減少すること
にある。このため近年では、酸素源である酸化鉄の一部
を気体酸素に代替して吹き込むことにより溶銑温度を補
償する方法もとられるようになってきた。
2. Description of the Related Art At present, a process for preliminarily desiliconizing, dephosphorizing and desulfurizing hot metal before charging into a converter and performing only decarburization in the converter to reduce the total cost of the refining process has become widespread. doing. In pre-siliconization and dephosphorization of hot metal, hot metal charged in a topped car or hot metal pot
A method of immersing a lance and blowing a dephosphorizing agent such as solid oxide containing iron oxide as a main component (hereinafter referred to as solid oxygen) and quicklime through a consumable immersion lance has been often used. The biggest weakness of this process is that the temperature of hot metal drops significantly due to the heat of decomposition of solid oxygen and the increase in sensible heat of solid oxygen and quicklime, and the heat margin in the converter, which is the next step, decreases. For this reason, in recent years, a method of compensating the hot metal temperature by replacing part of the iron oxide as an oxygen source with gaseous oxygen and injecting it has been adopted.

【0003】この際、気体酸素が溶銑中の各種成分と反
応する際に生じる酸化反応熱は極めて大きいため、酸素
源として固体酸素のみを用いた場合と同じ吹込方法を採
用したならばランス寿命の大幅な低下はまぬがれず工業
的な適用は困難とされてきた。そこでランス寿命を延長
させることを目的として、二重管ランスを用い、内管よ
り気体酸素、外管より不活性ガスで搬送した固体酸素お
よび生石灰等を吹き込む方法およびランス構造に関する
技術が特公昭61−24451 号公報、特公平2−25406 号公
報、特公平2−55485 号公報等に開示されている。これ
らの方法によれば確かにランス寿命は延長するものの、
ランス構造が複雑になるためランス1本当りのコストは
単管型のものに比べ4〜30倍にも上昇する。またランス
を二重管にすることで必然的にランス径の拡大を余儀な
くされ、その結果ランス重量の大幅な上昇、それに伴う
ランス交換作業の負荷増大といった問題が生じている。
[0003] At this time, since the heat of oxidation reaction generated when gaseous oxygen reacts with various components in the hot metal is extremely large, if the same blowing method as when only solid oxygen is used as the oxygen source is adopted, the lance life will be shortened. Significant decline has been expected and industrial application has been considered difficult. Therefore, in order to extend the life of the lance, a method of injecting gaseous oxygen from the inner tube, solid oxygen and quick lime conveyed by inert gas from the outer tube, and technology related to the lance structure using a double-tube lance and technology related to the lance structure have been proposed. No. 24451, Japanese Patent Publication No. 2-25406, Japanese Patent Publication No. 2-55485, and the like. Although these methods certainly extend the lance life,
Due to the complicated lance structure, the cost per lance increases by 4 to 30 times as compared with the single tube type. In addition, the use of a double-lance lance inevitably increases the diameter of the lance, resulting in a significant increase in the weight of the lance and a resulting increase in the load of lance replacement work.

【0004】また、固体酸素と生石灰を浸漬ランスより
吹き込むとともに気体酸素を浴表面に吹き付け、主とし
て浴中から発生するCOガスの二次燃焼により溶銑温度の
補償を図る方法も知られている。この方法では浸漬ラン
スの溶損の問題はないが、トピードカー等の炉口耐火物
の損耗が著しい、あるいは操業中のスプラッシュの発生
が激しいといった問題があった。
There is also known a method in which solid oxygen and quick lime are blown from an immersion lance and gaseous oxygen is blown onto a bath surface to compensate for hot metal temperature mainly by secondary combustion of CO gas generated in the bath. Although this method does not have the problem of erosion of the immersion lance, it has a problem that refractory at the furnace mouth such as a topped car is significantly worn or splash is generated during operation.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、前記
問題点を解決し、ランスコストが安価で、かつ作業負荷
の少ない単管ランスの長所を生かしつつ、工業的に適用
可能なランス寿命を確保して固体酸素の気体酸素への代
替による溶銑の温度補償を可能とする技術を提供するこ
とである。
SUMMARY OF THE INVENTION It is an object of the present invention to solve the above-mentioned problems and to make use of the advantages of a single-pipe lance with a low lance cost and a small work load, while maintaining an industrially applicable lance life. It is an object of the present invention to provide a technology which enables temperature compensation of hot metal by substituting solid oxygen with gaseous oxygen while securing the temperature.

【0006】[0006]

【課題を解決するための手段】すなわち本発明は、溶銑
中に酸化鉄を主成分とする固体酸化物および生石灰等の
脱燐剤からなる粉体を不活性ガス又は空気で搬送して吹
き込むと同時に気体酸素を吹き込んで溶銑の脱珪、脱燐
を行うに際して、単管の浸漬ランスをランスホルダーで
把持し、該ランスホルダーを内管と外管とからなる二重
管とし、それぞれの上端部近傍において互いに独立した
酸素吹込用配管および粉体吹込用配管と接続し、該内管
の下端を該単管の浸漬ランス内又は該ランスホルダー内
で開口させ、前記粉体の供給速度Qflux(kg/min )と
前記気体酸素の供給速度QO2(Nm3 /min )の比、Qfl
ux/QO2を6以上とし、前記粉体と前記気体酸素を予
め、該単管の浸漬ランス内または該ランスホルダー内で
混合してから溶銑中に吹き込むことを特徴とする溶銑の
脱珪、脱燐方法である。
That is, the present invention relates to a method of transporting and blowing a powder comprising a solid oxide containing iron oxide as a main component and a dephosphorizing agent such as quicklime into hot metal with an inert gas or air. When degassing and dephosphorizing hot metal by simultaneously injecting gaseous oxygen, the immersion lance of a single tube is gripped by a lance holder, and the lance holder is formed as a double tube consisting of an inner tube and an outer tube. In the vicinity, the pipe is connected to an independent oxygen blowing pipe and a powder blowing pipe, and the lower end of the inner pipe is opened in the immersion lance or the lance holder of the single pipe, and the powder supply rate Qflux (kg / Min) and the rate of supply of gaseous oxygen QO 2 (Nm 3 / min), Qfl
ux / QO 2 is 6 or more, and the powder and the gaseous oxygen are mixed in advance in the immersion lance or the lance holder of the single pipe and then blown into the hot metal, This is a dephosphorization method.

【0007】[0007]

【作用】以下、図1乃至図4を用い、本発明について説
明する。図1及び図3はトピードカーに充填された溶銑
へ気体酸素と固体酸素および生石灰等からなる粉体を吹
き込む場合に本発明を適用した様子を模式的に示したも
のである。粉体切出装置1内に払出された固体酸素2お
よび同様に粉体切出装置3内に払出された生石灰を主成
分とする脱燐剤4は、粉体吹込ライン5内を空気あるい
は窒素により搬送され、ランスホルダー7の内管へと供
給される。一方気体酸素は、酸素用配管6より7の外管
へと供給される。このようにして別個に供給された粉体
と気体酸素はランスホルダー7の下流部分乃至浸漬ラン
ス8内で混合された後、単管の浸漬ランス8を通じてト
ピードカー9に充填された溶銑10へ吹き込まれる。
The present invention will be described below with reference to FIGS. FIGS. 1 and 3 schematically show a state in which the present invention is applied to a case where a powder composed of gaseous oxygen, solid oxygen, quicklime, and the like is blown into hot metal filled in a tope car. The solid oxygen 2 discharged into the powder cutting device 1 and the dephosphorizing agent 4 mainly composed of quicklime discharged into the powder cutting device 3 likewise pass through the powder blowing line 5 with air or nitrogen. And is supplied to the inner tube of the lance holder 7. On the other hand, gaseous oxygen is supplied from the oxygen pipe 6 to the outer pipe 7. The powder and the gaseous oxygen separately supplied in this manner are mixed in the downstream portion of the lance holder 7 or in the immersion lance 8, and then blown into the hot metal 10 filled in the torpedo car 9 through the single tube immersion lance 8. .

【0008】ランスホルダーの構造例として、その拡大
図を図2および図4に示す。粉体は空気、窒素等に搬送
されて粉体導入管11からそれに接続されたランスホルダ
ー内管12へと供給される。一方気体酸素は、酸素導入用
のT字管13よりランスホルダー内管12とランスホルダー
外管14の間隙を通じて供給される。ここでランスホルダ
ー内管12は外管14よりも図2のように長い管で構成さ
れ、内管12の先端は浸漬ランス8内に突出した構造とな
り、粉体と気体酸素が浸漬ランス8内で混合されるか、
又は図4のように内管12は外管14よりも、短い管で構成
され、内管12が外管14内に開口して外管14のみの単管と
なった部分で粉体と気体酸素が混合される。このように
して混合された粉体と気体酸素はランスホルダーの外管
14と単管型の浸漬ランス8の接続部15を通じて少なくと
も浸漬ランス8内へ供給される。上記の例では粉体がラ
ンスホルダーの内管を、気体酸素が外管を通じて供給さ
れる例を示したが、本発明はこれに限るものではなく、
この構成が逆であっても特に問題とはならない。この点
に関しては既設の配管等の取合いから任意に定められる
ものと考えられる。
FIGS. 2 and 4 show enlarged views of an example of the structure of the lance holder. The powder is conveyed by air, nitrogen, or the like, and supplied from the powder introduction tube 11 to the lance holder inner tube 12 connected thereto. On the other hand, gaseous oxygen is supplied from a T-tube 13 for oxygen introduction through a gap between the inner tube 12 and the outer tube 14 of the lance holder. Here, the inner tube 12 of the lance holder is constituted by a tube longer than the outer tube 14 as shown in FIG. 2, and the tip of the inner tube 12 has a structure protruding into the immersion lance 8, so that powder and gaseous oxygen Mixed with
Alternatively, as shown in FIG. 4, the inner pipe 12 is formed of a shorter pipe than the outer pipe 14, and the inner pipe 12 is opened into the outer pipe 14 to form a single pipe of the outer pipe 14. Oxygen is mixed. The powder and gaseous oxygen mixed in this way are transferred to the outer tube of the lance holder.
It is supplied at least into the immersion lance 8 through the connection portion 15 of the single-tube type immersion lance 8. In the above example, the powder was supplied through the inner tube of the lance holder, and gas oxygen was supplied through the outer tube.However, the present invention is not limited to this.
Even if this configuration is reversed, there is no particular problem. It is considered that this point is arbitrarily determined based on the arrangement of the existing pipes and the like.

【0009】ところで、前述したように粉体と気体酸素
を混合して搬送した場合、配管の火災、爆発事故を引起
こす危険性が高くなることが指摘されてきた。そのため
もあって従来は二重管構造の浸漬ランスが用いられてき
たわけであるが、本発明者らは過去の酸素配管における
事故例、文献を詳細に調査するとともに、実験室規模の
実験を行うことにより、粉体と気体酸素の混合部がラン
スホルダー以降であれば、浸漬ランスが単管であって
も、配管火災、爆発事故の危険性は二重管ランスを用い
た場合と変わりがないことを明らかにした。
However, it has been pointed out that, as described above, when powder and gaseous oxygen are mixed and transported, there is a high risk of causing a fire or explosion accident in the piping. For this reason, immersion lances with a double-tube structure have been used in the past.However, the present inventors investigate past accidents and documents in oxygen piping in detail and conduct laboratory-scale experiments. Therefore, if the mixing part of powder and gaseous oxygen is after the lance holder, even if the immersion lance is a single pipe, the risk of pipe fire and explosion accident is the same as when using a double pipe lance It revealed that.

【0010】すなわち配管火災、爆発となる起点は、
1)配管の曲がり部等、粉体が管壁に激しく衝突する部
位、2)配管内に流れの死所が形成された際に、その部
分に管の摩耗等で発生した鉄粉などの可燃物が滞積した
場合、3)管内に油分や可燃性の洗浄剤が多量に付着し
た場合、4)可燃性のガスケットを用いた場合に帰着す
ることがわかった。
[0010] That is, the starting point of pipe fire and explosion is:
1) A part where the powder violently collides with the pipe wall, such as a bent part of the pipe. 2) When a dead space of the flow is formed in the pipe, flammable iron powder or the like generated at that part by abrasion of the pipe. It was found that the accumulation was caused by 3) the oil and the flammable cleaning agent adhered to the pipe in a large amount, and 4) the flammable gasket was used.

【0011】従って本発明のように上記の4つの要因を
回避すれば、浸漬ランスが単管構造であっても全て問題
は解決される。なお、さらに万全を期すためには、ラン
スホルダー構造も含めて、粉体の搬送系路はできる限り
直線状にするとともに、ランスホルダーおよびランスを
構成する材料には何らかの表面硬化処理を施すことが望
ましい。
Therefore, if the above four factors are avoided as in the present invention, all problems can be solved even if the immersion lance has a single tube structure. In order to further ensure thoroughness, the conveying system for the powder, including the lance holder structure, should be made as straight as possible, and the material forming the lance holder and the lance should be subjected to some surface hardening treatment. desirable.

【0012】またランスホルダー内管12の浸漬ランス8
内への突出長さに関しては、特別規定するものではない
が、浸漬ランスが消耗した際に、ランスホルダー内管が
溶銑に直接接触することのないよう、ランスを最下限に
まで浸漬させた場合に、浴表面より上部に位置するもの
であれば良い。また、ランスホルダー外管の形状に関し
ては先端の径を若干絞った例を示したが、この点も特に
規定されるものではなく、操業条件に応じて必要量の気
体酸素および粉体の供給速度が確保できるよう、任意に
設計すれば良い。
Also, the immersion lance 8 of the inner tube 12 of the lance holder.
The length of protrusion into the lance is not specified, but when the lance is exhausted, the lance is immersed to the lowest limit so that the inner tube of the lance does not come into direct contact with the hot metal. What is necessary is just to be located above the bath surface. In addition, the example of the shape of the outer tube of the lance holder was described in which the diameter of the tip was slightly narrowed, but this point is not particularly specified, and the supply rate of the required amount of gaseous oxygen and powder in accordance with the operating conditions. May be arbitrarily designed so as to secure

【0013】また一方ランスホルダー内管のホルダー内
での長さに関しても特別規定するものではないが、別個
に供給された粉体および気体酸素がそれぞれランスホル
ダー内外管で下流方向へ整流されるに充分な距離だけを
最低確保すれば良い。ランスホルダーの形状について
は、先端の径をランス径と同等程度まで絞った例を示し
たが、この点も特別に規定されるものではなく、操業条
件に応じて必要量の気体酸素および供給速度が確保でき
るよう任意に設計すれば良い。
On the other hand, the length of the inner tube of the lance holder is not specially specified, but the powder and gaseous oxygen supplied separately are rectified downstream by the inner and outer tubes of the lance holder, respectively. You only need to secure a minimum of a sufficient distance. Regarding the shape of the lance holder, an example was shown in which the diameter of the tip was reduced to about the same as the lance diameter, but this point is also not specially specified. May be arbitrarily designed so that

【0014】さてこのようにして混合された気体酸素と
粉体は単管の浸漬ランスを通じて溶銑中に吹き込まれる
わけであるが、前述したように、従来単管ランスで気体
酸素を吹き込む場合、ランスの溶損が著しく工業的に成
り立たないとされてきた。しかしながら、本発明者らは
一方で、固体酸素の分解熱および固体酸素と生石灰等の
脱燐材の顕熱増が、ランス出口近傍の冷却効果を有し、
結果的にランスの溶損を抑制することに着目した。具体
的なデータは後に示すが、結論としては固体酸素および
生石灰等の脱燐剤からなる粉体と、気体酸素について、
それぞれの供給速度の比Qflux/QO2を6以上とすれ
ば、単管ランスにおいても、工業的に成立可能な程度に
までランスの溶損が抑制できることを見出した。
The gaseous oxygen and the powder thus mixed are blown into the hot metal through a single-tube immersion lance. As described above, when gaseous oxygen is blown with a conventional single-tube lance, It has been said that the erosion of steel is not industrially feasible. However, the present inventors meanwhile, the heat of decomposition of solid oxygen and the increase in sensible heat of the dephosphorizing material such as solid oxygen and quick lime have a cooling effect near the lance outlet,
As a result, we focused on suppressing the melting of the lance. Specific data will be shown later, but the conclusion is that powder consisting of solid oxygen and dephosphorizing agent such as quicklime and gaseous oxygen
If each of the feed rate ratio Qflux / QO 2 to 6 or more, even in a single tube lance, erosion of the lance until the industrially extent possible satisfied found that can be suppressed.

【0015】以上本発明についてトピードカーに充填さ
れた溶銑に斜め向きにランスを浸漬した場合を示した
が、容器はトピードカーに限るものではなく溶銑鍋等の
ものでも良く、ランスの浸漬角度も斜めに限るものでは
ない。以下、実施例に基づいて本発明をより詳細に説明
する。
In the present invention, the case where the lance is immersed obliquely in the hot metal filled in the tope car has been described. However, the container is not limited to the tope car and may be a hot metal pot or the like. It is not limited. Hereinafter, the present invention will be described in more detail based on examples.

【0016】[0016]

【実施例】装置の構成は、実施例1では図1および図2
に、実施例2では図3および図4に示したものと基本的
に同一である。また比較例として二重管ランスを用いた
実験も行った。比較例における装置の概略図を図7に示
す。この例においては、ランスホルダーは全区間二重管
となっており、ランスホルダーの内管に同径の鋼管を、
外管に外表面を耐火皮覆した鋼管をそれぞれ接続し全区
間二重管の浸漬ランスを構成した。なお、ここでは前述
の二重管ランスを用いた従来技術に従い、外管より粉体
を、内管より気体酸素を供給した。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In the first embodiment, the structure of the apparatus is shown in FIGS.
The second embodiment is basically the same as that shown in FIGS. As a comparative example, an experiment using a double tube lance was also performed. FIG. 7 is a schematic diagram of an apparatus in a comparative example. In this example, the lance holder is a full section double pipe, and a steel pipe of the same diameter is used for the inner pipe of the lance holder.
Steel pipes whose outer surfaces were covered with fire-resistant skin were connected to the outer pipes, respectively, to form a immersion lance for the double pipes in all sections. Here, powder was supplied from the outer tube and gaseous oxygen was supplied from the inner tube according to the conventional technique using the above-described double tube lance.

【0017】表1に実施例および比較例におけるランス
の諸元を示す。なお比較例のランス径等は実施例におけ
る装置と同等の吹込条件が得られるよう設計した。実施
例および比較例における標準的な操業条件を表2に示
す。この条件で操業した場合のランス寿命、ランスコス
トおよびランス交換時間の比較を表3に示す。実施例の
場合、ランス寿命は若干短くなるものの、1本当りのコ
ストが安いため、処理に要するランスコストは半分以下
になる。また構造が簡単かつランス重量が軽いため、ラ
ンス交換作業が容易となり交換時間は比較例に比べ約1
/4〜1/5で済むことがわかる。さらに図5には実施
例および比較例における脱珪外脱燐酸素効率と溶銑中燐
濃度の関係を示す。
Table 1 shows the specifications of the lance in Examples and Comparative Examples. The lance diameter and the like of the comparative example were designed so as to obtain the same blowing conditions as those of the apparatus in the example. Table 2 shows standard operating conditions in Examples and Comparative Examples. Table 3 shows a comparison of lance life, lance cost, and lance replacement time when operated under these conditions. In the case of the embodiment, although the lance life is slightly shortened, the cost per lance is low, so the lance cost required for processing is less than half. Further, since the structure is simple and the lance weight is light, the lance replacement operation is easy, and the replacement time is about one time as compared with the comparative example.
It can be seen that で to 5 is enough. FIG. 5 shows the relationship between the desiliconization external dephosphorization oxygen efficiency and the phosphorus concentration in the hot metal in Examples and Comparative Examples.

【0018】実施例では、比較例に比べて5%程度脱燐
効率が向上することがわかる。一般的に脱燐反応効率の
向上には、反応サイトに生石灰等の脱燐剤と酸素源を共
存させることが重要とされている。従って実施例の場
合、ランスホルダーおよびランス内で気体酸素と粉体が
充分に混合された状況で吹き込まれたため、反応効率が
向上したものと考えられる。
It can be seen that in the example, the dephosphorization efficiency is improved by about 5% as compared with the comparative example. In general, it is important to coexist a dephosphorizing agent such as quicklime and an oxygen source at a reaction site in order to improve the dephosphorization reaction efficiency. Therefore, in the case of the embodiment, it is considered that the reaction efficiency was improved because the gas was blown in a state where the gaseous oxygen and the powder were sufficiently mixed in the lance holder and the lance.

【0019】前述したように本発明の方法によるランス
寿命の確保は、固体酸素の分解熱および固体酸素と生石
灰等の脱燐剤の顕熱増に伴うランス出口近傍の冷却効果
に共存するものである。本発明者らは前記の操業条件を
基準として気体酸素および粉体の供給速度を様々に変化
させて、ランス溶損状況を詳細に調査した。その結果、
図6に示すようにランスの溶損速度は、粉体と気体酸素
の供給速度の比により、良く整理されることがわかっ
た。
As described above, the securing of the lance life by the method of the present invention coexists with the heat of decomposition of solid oxygen and the cooling effect near the lance outlet due to the increase in sensible heat of the solid oxygen and the dephosphorizing agent such as quicklime. is there. The inventors of the present invention varied the supply rates of the gaseous oxygen and the powder based on the above-mentioned operating conditions, and investigated the lance erosion state in detail. as a result,
As shown in FIG. 6, it was found that the lance melting rate was well controlled by the ratio of the powder and gaseous oxygen supply rates.

【0020】本発明が工業的に成立するためには、望ま
しくは1本のランスで少なくとも1回の処理をまかなう
必要がある。一方、一般的な脱珪・脱燐処理時間が10〜
30分、その際のランスの浸漬深さが1000〜1500mmである
ことを考慮すれば、ランスの溶損速度を最大50mm/min
程度に抑える必要がある。図6に示した関係からランス
溶損速度を50mm/min 以下に抑えるためには、粉体と気
体酸素の供給速度の比を6以上に設定するのがよいこと
がわかる。
In order for the present invention to be industrially feasible, it is desirable that at least one treatment be performed with one lance. On the other hand, general desiliconization / dephosphorization processing time is 10 ~
Taking into account that the immersion depth of the lance at that time is 1000 to 1500 mm, the melting speed of the lance is 50 mm / min at the maximum.
It is necessary to suppress to the extent. From the relationship shown in FIG. 6, it can be seen that in order to suppress the lance melting speed to 50 mm / min or less, it is better to set the ratio of the supply speed of the powder and gaseous oxygen to 6 or more.

【0021】[0021]

【表1】 [Table 1]

【0022】[0022]

【表2】 [Table 2]

【0023】[0023]

【表3】 [Table 3]

【0024】[0024]

【発明の効果】本発明は、固体酸素および生石灰等の脱
燐剤からなる粉体と気体酸素を独立にそれぞれ二重管か
らなるランスホルダーで搬送し、粉体と気体酸素の供給
速度の比を6以上として、単管の浸漬ランス内又はラン
スホルダー内で混合し、単管の浸漬ランスから溶銑中に
吹き込んで脱珪・脱燐を行うもので、工業的に成立可能
な程度にまでランスの溶損を抑えることができ、しかも
従来の二重管方式のランスを用いた場合に比べて大幅な
ランスコストの削減およびランス交換作業負荷の低減が
可能となった。
According to the present invention, a powder comprising a dephosphorizing agent such as solid oxygen and quicklime and gaseous oxygen are independently transported by a lance holder comprising a double tube, and a ratio of the supply speed of the powder to gaseous oxygen is obtained. 6 or more, mixed in a single-tube immersion lance or lance holder, and blown into hot metal from a single-tube immersion lance to perform desiliconization and dephosphorization. The lance can be suppressed from being melted, and the lance cost and the lance replacement work load can be significantly reduced as compared with the case where a conventional double-tube lance is used.

【0025】また、気体酸素と粉体との混合が良好なた
め、脱燐反応効率が向上するという効果も有する。
Further, since the mixing of the gaseous oxygen and the powder is good, there is an effect that the dephosphorization reaction efficiency is improved.

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

【図1】本発明の実施に好適な1装置構成を示す概念図
である。
FIG. 1 is a conceptual diagram showing one device configuration suitable for implementing the present invention.

【図2】本発明の実施に好適なランスホルダーの1構造
を示す断面図である。
FIG. 2 is a sectional view showing one structure of a lance holder suitable for carrying out the present invention.

【図3】本発明の実施に好適な1装置構成を示す概念図
である。
FIG. 3 is a conceptual diagram showing one device configuration suitable for implementing the present invention.

【図4】本発明の実施に好適なランスホルダーの1構造
を示す断面図である。
FIG. 4 is a sectional view showing one structure of a lance holder suitable for carrying out the present invention.

【図5】実施例および比較例における脱珪外脱燐酸素効
率と溶銑中燐濃度の関係を示すグラフである。
FIG. 5 is a graph showing the relationship between desiliconization dephosphorization oxygen efficiency and phosphorus concentration in hot metal in Examples and Comparative Examples.

【図6】本発明におけるランス溶損速度と、気体酸素の
供給速度に対する粉体の供給速度の比の関係を示すグラ
フである。
FIG. 6 is a graph showing a relationship between a lance melting rate and a ratio of a powder supply rate to a gas oxygen supply rate in the present invention.

【図7】比較例に用いた装置構成を示す概念図である。FIG. 7 is a conceptual diagram illustrating a device configuration used in a comparative example.

【符号の説明】[Explanation of symbols]

1 粉体切出装置 2 固体酸素 3 粉体切出装置 4 脱燐剤 5 粉体吹込用配管 6 気体酸素用配管 7 ランスホルダー 8 浸漬ランス 9 トピードカー 10 溶銑 11 粉体導入管 12 ランスホルダー内管 13 気体酸素導入用T字管 14 ランスホルダー外管 15 ランス接続部 DESCRIPTION OF SYMBOLS 1 Powder extraction apparatus 2 Solid oxygen 3 Powder extraction apparatus 4 Dephosphorizer 5 Powder injection pipe 6 Gas oxygen pipe 7 Lance holder 8 Immersion lance 9 Topy car 10 Hot metal 11 Powder introduction pipe 12 Lance holder inner pipe 13 T-tube for introducing gaseous oxygen 14 Lance holder outer tube 15 Lance connection

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭62−185814(JP,A) 特公 昭62−6608(JP,B2) 実公 平2−4113(JP,Y2) (58)調査した分野(Int.Cl.6,DB名) C21C 1/04 101 C21C 1/02 110 F27D 3/18──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-62-185814 (JP, A) JP-B-62-6608 (JP, B2) Jiko 2-4113 (JP, Y2) (58) Field (Int.Cl. 6 , DB name) C21C 1/04 101 C21C 1/02 110 F27D 3/18

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 溶銑中に酸化鉄を主成分とする固体酸化
物および生石灰等の脱燐剤からなる粉体を不活性ガス又
は空気で搬送して吹き込むと同時に気体酸素を吹き込ん
で溶銑の脱珪、脱燐を行うに際して、単管の浸漬ランス
をランスホルダーで把持し、該ランスホルダーを内管と
外管とからなる二重管とし、それぞれの上端部近傍にお
いて互いに独立した酸素吹込用配管および粉体吹込用配
管と接続し、該内管の下端を該単管の浸漬ランス内で開
口させ、前記粉体の供給速度Qflux(kg/min )と前記
気体酸素の供給速度QO2(Nm3 /min )の比、Qflux/
QO2を6以上とし、前記粉体と前記気体酸素を予め、該
単管の浸漬ランス内で混合してから溶銑中に吹き込むこ
とを特徴とする溶銑の脱珪、脱燐方法。
An inert gas or air is used to convey and blow a powder comprising a solid oxide containing iron oxide as a main component and a dephosphorizing agent such as quicklime into the hot metal, and simultaneously blows gaseous oxygen to remove the hot metal. When performing silicon and dephosphorization, a single pipe immersion lance is gripped by a lance holder, and the lance holder is formed as a double pipe consisting of an inner pipe and an outer pipe. And the lower end of the inner pipe is opened in the immersion lance of the single pipe, and the powder supply rate Qflux (kg / min) and the gas oxygen supply rate QO 2 (Nm 3 / min), Qflux /
A method for desiliconizing and dephosphorizing hot metal, wherein QO 2 is 6 or more, and the powder and the gaseous oxygen are mixed in advance in a dipping lance of the single tube and then blown into the hot metal.
【請求項2】 溶銑中に酸化鉄を主成分とする固体酸化
物および生石灰等の脱燐剤からなる粉体を不活性ガス又
は空気で搬送して吹き込むと同時に気体酸素を吹き込ん
で溶銑の脱珪、脱燐を行うに際して、単管の浸漬ランス
をランスホルダーで把持し、該ランスホルダーを内管と
外管とからなる二重管とし、それぞれの上端部近傍にお
いて互いに独立した酸素吹込用配管および粉体吹込用配
管と接続し、該内管の下端を該ランスホルダーに開口さ
せ、前記粉体の供給速度Qflux(kg/min )と前記気体
酸素の供給速度QO2(Nm3 /min )の比、Qflux/QO2
を6以上とし、前記粉体と前記気体酸素を予め、該ラン
スホルダー内で混合してから溶銑中に吹き込むことを特
徴とする脱珪、脱燐方法。
2. A method for removing hot metal by feeding powder containing a solid oxide containing iron oxide as a main component and a dephosphorizing agent such as quick lime into the hot metal with an inert gas or air and simultaneously blowing gaseous oxygen into the hot metal. When performing silicon and dephosphorization, a single pipe immersion lance is gripped by a lance holder, and the lance holder is formed as a double pipe consisting of an inner pipe and an outer pipe. And the lower end of the inner pipe is opened to the lance holder, and the powder supply rate Qflux (kg / min) and the gas oxygen supply rate QO 2 (Nm 3 / min) Ratio, Qflux / QO 2
Wherein the powder and the gaseous oxygen are preliminarily mixed in the lance holder and then blown into the hot metal.
JP5068313A 1993-03-26 1993-03-26 Hot metal desiliconization and dephosphorization method Expired - Fee Related JP2812852B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5068313A JP2812852B2 (en) 1993-03-26 1993-03-26 Hot metal desiliconization and dephosphorization method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5068313A JP2812852B2 (en) 1993-03-26 1993-03-26 Hot metal desiliconization and dephosphorization method

Publications (2)

Publication Number Publication Date
JPH06279825A JPH06279825A (en) 1994-10-04
JP2812852B2 true JP2812852B2 (en) 1998-10-22

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Country Link
JP (1) JP2812852B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013209737A (en) * 2011-04-27 2013-10-10 Jfe Steel Corp Method for producing molten steel
CN103540708B (en) * 2013-10-14 2015-09-09 北京科技大学 Nano-meter SiO_2 is reclaimed in a kind of molten iron gasification desiliconization 2method

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS626608A (en) * 1985-07-02 1987-01-13 ヤンマー農機株式会社 Apparatus for automatic control of handling depth
JPS62185814A (en) * 1986-02-10 1987-08-14 Sumitomo Metal Ind Ltd Lance
JPH024113U (en) * 1988-06-22 1990-01-11

Also Published As

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