JPS59104414A - Method for desiliconization of molten iron - Google Patents

Method for desiliconization of molten iron

Info

Publication number
JPS59104414A
JPS59104414A JP21337982A JP21337982A JPS59104414A JP S59104414 A JPS59104414 A JP S59104414A JP 21337982 A JP21337982 A JP 21337982A JP 21337982 A JP21337982 A JP 21337982A JP S59104414 A JPS59104414 A JP S59104414A
Authority
JP
Japan
Prior art keywords
molten iron
runner
desiliconizing
cylindrical
desiliconization
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.)
Pending
Application number
JP21337982A
Other languages
Japanese (ja)
Inventor
Kazuo Ogahira
大河平 和男
Arata Tanaka
新 田中
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.)
Nippon Steel Corp
Original Assignee
Nippon 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP21337982A priority Critical patent/JPS59104414A/en
Publication of JPS59104414A publication Critical patent/JPS59104414A/en
Pending 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
    • C21C1/00Refining of pig-iron; Cast iron
    • C21C1/04Removing impurities other than carbon, phosphorus or sulfur

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

Abstract

PURPOSE:To stabilize the efficiency of desiliconizing reaction at a high level, by adjusting the ratio of the running out speed of molten iron falling from a casting bed runner to a tilting runner and the passage sectional area of cylindrical molten iron passage body to a speific range in carrying out the desiliconization of molten iron by providing the cylindrical molten iron passage body between the casting bed runner of blast furnace and the tilting runner. CONSTITUTION:A cylindrical molten iron passage body 8, for example, discontinuously composed of refractory is provided to the casting bed runner 2 and between the blast furnace casting bed runner 2 and the tilting runner 3. The molten iron flow 7 containing desiliconizing agent is tapped into the tilting runner 3 via the cylindrical molten iron passage body 8 and the desiliconization of molten iron is carried out. In that time, the ratio of the tapping speed (kg/ min) and the passage sectional area (cm<2>) of cylindrical molten iron passage body shall be in a range of 2 to 20. When this ratio is <=2, sufficient desiliconizing oxygen efficiency can not be obtained and when it is >2, overflow of the molten metal is feared.

Description

【発明の詳細な説明】 本発明は高炉鋳床での溶銑脱珪を効率よく安定して行な
わしめることを目的とした溶銑脱珪処理法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a hot metal desiliconization treatment method aimed at efficiently and stably desiliconizing hot metal in a blast furnace casthouse.

近年、溶鋼の高純度化、製品の高級化にともない、ソー
ダ灰や石灰系7/−ソクスによる溶銑の予備脱リン・脱
硫処理が行なわれている。この溶銑脱リン・脱硫処理に
おいては、溶銑Siはできるだけ低いことが好ましく、
少くとも0・15%以下に脱珪する必要がある。
In recent years, with the increasing purity of molten steel and the upgrading of products, preliminary dephosphorization and desulfurization treatment of molten pig iron using soda ash or lime-based 7/-sox has been carried out. In this hot metal dephosphorization/desulfurization treatment, it is preferable that the hot metal Si content is as low as possible.
It is necessary to remove silicon to at least 0.15% or less.

従来、溶銑脱珪法としては、溶銑の自然落下エネルギー
を利用した高炉鋳床溶銑樋部での鋳床脱珪方法が周知で
ある。
BACKGROUND ART Conventionally, as a hot metal desiliconization method, a method for desiliconizing a cast bed in a blast furnace cast bed hot metal trough part using the natural falling energy of hot metal is well known.

この鋳床脱珪法は、第1図に示す如く、高炉1から流出
した溶銑が鋳床樋2、傾注樋3を経てトビードカー4内
に導かれる過程で、ホツノぐ一5内に貯蔵された脱珪剤
(酸化鉄)をフィーダー6を介して鋳床樋2内の溶銑流
上に供給されるものであることから、鋳床樋では溶銑と
脱珪剤との混合攪拌作用が小さく、供給した脱珪剤はそ
の大部分が溶銑の上に浮い次状態で、次の傾注樋3内に
自然落下され、その位置エネルギーによって攪拌混合さ
れ脱珪反応が進行する。
As shown in Fig. 1, in this casting bed desiliconization method, hot metal flowing out from the blast furnace 1 is guided into the tobeed car 4 via the cast bed gutter 2 and the tilting gutter 3, and is stored in the hot iron 5. Since the desiliconizing agent (iron oxide) is fed onto the flow of hot metal in the cast bed trough 2 through the feeder 6, the mixing and stirring action of the molten metal and the desiliconizing agent in the cast bed trough is small, and the supply is slow. The desiliconizing agent, most of which floats on top of the hot metal, falls naturally into the next tilting trough 3, where it is stirred and mixed by its potential energy, and the desiliconizing reaction proceeds.

従って、上述した従来の鋳床脱珪法は、自由落下方式で
オシ、落下流のいわゆる滝つぼ近傍のみでの攪拌混合で
あるため脱珪剤と溶銑間の攪拌混合が不十分であシ脱珪
反応効率に低く、パラクキが大きい欠点がある。
Therefore, the conventional castbed desiliconization method described above uses a free-fall method and stirs and mixes only near the so-called waterfall basin of the falling flow, so stirring and mixing between the desiliconizing agent and the hot metal is insufficient. It has the drawbacks of low reaction efficiency and large fluctuations.

さらに従来の鋳床脱珪法のもう−っの欠点は傾注樋3か
らトピードヵ−4に溶銑が注入された段階で、未反応の
酸化鉄(脱珪剤)にょる脱炭反応によってトピードヵー
4内でのスラグフォーミングが大きく、従って、供給酸
化鉄量に制約が生じ、Siを低位に安定して処理するこ
とを不可能にしている点である。
Furthermore, another drawback of the conventional castbed desiliconization method is that when hot metal is injected from the tilting trough 3 into the torpedo car 4, the decarburization reaction caused by unreacted iron oxide (desiliconizing agent) The problem is that slag forming in the process is large, which limits the amount of iron oxide to be supplied, making it impossible to stably process Si to a low level.

本発明は従来の鋳床脱珪法における脱珪反応効率が低く
、かつ/々ラッキが大きい欠点およびトビードカー内で
のスラグ7オーミングが大きいという問題全解決すべく
なされたもので、その特徴とするところは、鋳床樋がら
傾注樋に脱珪剤を含む溶銑が落下する流路に、筒状溶湯
流路体を数例け、該筒状溶湯流路体を介して脱珪剤を加
えた溶銑全傾注樋内に導くことによって、脱珪剤き溶銑
との混合攪拌全強化し、脱珪反応全十分進行させ、バラ
ツキをなくし脱珪反応効率を高位安定させるとともに1
.トピードカー内でのスラグフォーミングを防止するこ
とを目的としたものである。
The present invention has been made to solve all the problems of the conventional cast bed desiliconization method, such as low desiliconization reaction efficiency and large racking, and large slag 7 ohming in the tobead car, and has the following characteristics: However, several cylindrical molten metal channel bodies were installed in the channel through which hot metal containing a desiliconizing agent falls into the tilting gutter from the casting bed gutter, and the desiliconizing agent was added through the cylindrical molten metal channel body. By introducing the hot metal fully into the tilting culvert, the mixing and stirring of the hot metal with the desiliconizing agent is fully intensified, the desiliconizing reaction fully progresses, and the dispersion is eliminated and the desiliconizing reaction efficiency is stabilized at a high level.
.. The purpose is to prevent slag forming inside the torpedo car.

而して、本発明者等は、本発明の完成に先立つて種々研
究全軍ねた結果、脱珪剤と溶銑の最適混合攪拌は、筒状
溶銑流路体の流路断面積(、y4)あたシの溶銑速度(
K9/m)の比が一定範囲にある場合に実現し得ること
を知見し得、本発明を完成したのである。
As a result of various researches conducted prior to the completion of the present invention, the present inventors found that the optimal mixing and stirring of the desiliconizing agent and hot metal is based on the channel cross-sectional area (, y4) of the cylindrical hot metal channel body. ) Atashi hot metal speed (
They found that this can be achieved when the ratio of K9/m) is within a certain range, and completed the present invention.

上記筒状溶湯流路体の具備すべき条件は、鋳床樋から傾
注樋へ落下する溶銑の流出速度W (Kg/―)と該筒
状溶湯流路体の流路断面積5(cfl)と比 の#ヰ(W/S)が2〜20になるように筒状溶湯流路
体の流路断面(内管)径を定めることである。
The conditions that the cylindrical molten metal channel body must meet are the outflow velocity W (Kg/-) of the hot metal falling from the casting bed trough to the tilting trough, and the channel cross-sectional area 5 (cfl) of the cylindrical molten metal channel body. The diameter of the channel cross section (inner tube) of the cylindrical molten metal channel body is determined so that the ratio #W/S is 2 to 20.

該筒状溶湯流路体の流路断面(内管)径が、上記指標の
20よシ大きい場合は、鋳床樋よ逆流出する溶銑と脱珪
剤とを該筒状流路体からオーバーフローさせることなく
傾注樋へ導くことが困難である。又該筒状溶湯流路体の
流路断面(内管)径が上記指標の2よシ小さい場合は、
脱珪剤と溶銑との混合攪拌が不十分で所期の目的を達成
することが出来ない。
If the diameter of the cross section (inner tube) of the cylindrical molten metal channel body is larger than the above index of 20, the molten metal and desiliconization agent flowing back from the cast bed gutter will overflow from the cylindrical channel body. It is difficult to guide it to the tilting gutter without causing it to drop. In addition, if the diameter of the channel cross section (inner pipe) of the cylindrical molten metal channel body is smaller than 2 of the above index,
The desired purpose cannot be achieved due to insufficient mixing and stirring of the desiliconizing agent and hot metal.

以下本発明を図面にもとづいて説明する。The present invention will be explained below based on the drawings.

第2図は本発明の実施例を示す説明図で、2は鋳床樋、
3は傾注樋、  7tri鋳床樋2の先端から傾注樋3
へ流出落下せる脱珪剤を含む溶銑流である。
FIG. 2 is an explanatory diagram showing an embodiment of the present invention, and 2 is a cast bed gutter;
3 is the tilting gutter, from the tip of the 7tri cast bed gutter 2 to the tilting gutter 3
This is a hot metal stream containing a desiliconizing agent that flows out and falls into the molten metal.

第2図(a)は、鋳床樋2と傾注樋3との間で、前記鋳
床樋に非連続で適宜支持部材によって、予め取付けられ
た筒状溶湯流路体例えば円筒状の耐火物管8を介して脱
珪剤を含む溶銑流7を傾注樋3へ導く溶銑脱珪法を示し
、また第2図(b)は鋳床槌2の先端に密着して、周囲
を鉄板で覆参た耐火物管9全取付け、鋳床@2よ逆流出
する脱珪剤を含む溶#7を該耐火物管9に連続して導く
溶銑脱珪法を示している。
FIG. 2(a) shows a cylindrical molten metal channel body, such as a cylindrical refractory, discontinuously attached to the cast bed gutter by an appropriate support member between the cast bed gutter 2 and the tilting gutter 3. A method of desiliconizing hot metal is shown in which the hot metal flow 7 containing a desiliconizing agent is guided to the tilting trough 3 through a pipe 8, and FIG. This figure shows a hot metal desiliconization method in which all the refractory pipes 9 are installed and melt #7 containing a desiliconizing agent flowing back from the cast bed @2 is continuously introduced into the refractory pipes 9.

実施例: 第2図(a)に示すような方法で、鋳床樋2と傾注@3
.!:の間に内径500 taxiの高アルミナ質耐火
物管を取付けs  10 Ton /=の出銑速度で該
耐火物管を介して連続25分間脱珪処理を行なった結果
全第1表に示す。
Example: In the method shown in Fig. 2(a), the cast bed trough 2 and the tilting @3
.. ! A high alumina refractory pipe with an inner diameter of 500 taxis was installed between the refractory pipes, and desiliconization was performed continuously for 25 minutes through the refractory pipe at a tapping rate of s 10 Ton /=.The results are shown in Table 1.

第  1  表 本実施例の脱珪処理法は従来法に比し脱珪効率が著しく
改善され、かつトピードカー内でのスラグ7オーミング
現象も認められなかった。
Table 1 The desiliconization treatment method of this example had significantly improved desiliconization efficiency compared to the conventional method, and no slag 7 ohming phenomenon was observed in the torpedo car.

このように高炉鋳床脱珪処理において、鋳床樋2から傾
注樋3に至る過程で、溶銑と脱珪剤との混合攪拌強化を
目的として用いられる本発明による筒状溶湯流路体8の
形状は、第2図(a)、第2図(1))の実施例に示し
た垂直管に限らず、屈折管や途中に内径の変化をもたせ
た管など、いわゆる溶銑と脱珪剤との混合攪拌をよシ強
化する目的で種々の改良を行った筒状溶湯流路体8を用
いることはより望丑しい。
As described above, in the desiliconization treatment of the blast furnace casthouse, the cylindrical molten metal channel body 8 according to the present invention is used for the purpose of strengthening the mixing and stirring of hot metal and the desiliconizing agent in the process from the casting bed trough 2 to the tilting trough 3. The shape is not limited to the vertical tube shown in the examples shown in Figure 2 (a) and Figure 2 (1)), but also bent tubes, tubes with a change in inner diameter in the middle, etc. It is more desirable to use a cylindrical molten metal channel body 8 that has undergone various improvements for the purpose of enhancing the mixing and agitation of the molten metal.

また、W/S (溶銑速度CKy/m+)/筒状溶湯流
路体の流路断面積(cnl )〕の選択は脱Si酸素効
率ならびに作業性の両面から本発明の重要々要件の一つ
である。
In addition, the selection of W/S (hot metal speed CKy/m+)/channel cross-sectional area of the cylindrical molten metal channel body (cnl)] is one of the important requirements of the present invention from both the Si removal oxygen efficiency and workability. It is.

部ちW/S<lては脱Si酸素効率の改善がほとんどな
い。
When W/S<l, there is almost no improvement in the Si removal oxygen efficiency.

またW / Sが大きくなると、第2図(a)の方式で
は浸m管断面積が溶銑量に対し小さくなるので、溶銑と
脱珪剤ならびに差込まれた空気によるガス発生によシ溶
針がオーツ々−フローすることがあり困 操業が相離に々る。したがってW/Sは2〜2゜の範囲
に選定されねばならない。
Furthermore, as W/S increases, in the method shown in Figure 2 (a), the cross-sectional area of the immersion pipe becomes smaller relative to the amount of hot metal, so the melting needle is However, the oats may flow, leading to difficult operations. Therefore, W/S must be selected within the range of 2 to 2 degrees.

この内特に望ましいのはW/Sは5〜10である。Among these, W/S of 5 to 10 is particularly desirable.

本発明は上述したように構成し且つ用いることにより脱
珪剤と溶銑の最適混合攪拌を実現し、これによって十分
な脱珪反応の進行全促し結局は脱硫反応効率全高位安定
させることが出来、しかもトビードカー内でのスラグフ
ォーミングを抑止するなど溶湯品質向上に加え作M I
I内向上も貢献するところがきわめて太きい。
By configuring and using the present invention as described above, it is possible to achieve optimal mixing and stirring of the desiliconizing agent and hot metal, thereby promoting the full progress of the desiliconizing reaction and ultimately stabilizing the overall desulfurization reaction efficiency. Moreover, in addition to improving the quality of molten metal by suppressing slag forming inside the tobeed car,
Improvements within I also make a huge contribution.

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

第1図は従来の筒炉鋳床脱珪処理工程の説明図、第2図
(a)、第2図(b)は本発明の鋳床脱珪処理工程の一
火施例を示す説明図である。 1・・・高炉、2・・・鋳床樋、3・・・傾注樋、4・
・・トビードカー、5・・・脱珪剤貯蔵ホツノξ−16
・・・フィーダー、7・・・脱珪剤を含む溶針流、8,
9・・・耐火物製筒状管。 代理人 弁理士  秋 沢 政 光 外2名
FIG. 1 is an explanatory diagram of a conventional cylindrical furnace casting bed desiliconization process, and FIGS. 2(a) and 2(b) are explanatory diagrams showing a one-fire example of the castbed desiliconization process of the present invention. It is. 1...Blast furnace, 2...Cast bed gutter, 3...Tilt gutter, 4...
・・Tobeed car, 5・・Siliconizing agent storage hottuno ξ-16
...feeder, 7...melting needle flow containing a desiliconizing agent, 8,
9... Cylindrical pipe made of refractory material. Agent: Patent attorney Masaaki Akizawa, Mitsugai (2 people)

Claims (1)

【特許請求の範囲】 (11高炉鋳床樋、傾注樋間に、前記高炉鋳床樋に連続
若しくは非連続に設けた筒状溶湯流路体を用いて溶銑の
脱珪全行なうにあたシ、脱珪剤を加えた溶銑を、 出銑速度(Kp/am)/筒状溶湯流路体の流路断面積
(,4) の比が2〜20の範囲で、前記筒状溶湯流路体を通過さ
せることを特徴とする溶銑の脱珪方法。
[Scope of Claims] (11) A system for completely desiliconizing hot metal using a cylindrical molten metal channel body provided between the blast furnace cast bed trough and the tilting trough, either continuously or discontinuously in the blast furnace cast bed trough. , hot metal to which a desiliconizing agent has been added is added to the cylindrical molten metal flow path at a ratio of tapping rate (Kp/am)/flow path cross-sectional area of the cylindrical molten metal flow path body (,4) in the range of 2 to 20. A method for desiliconizing hot metal, which is characterized by passing it through a body.
JP21337982A 1982-12-07 1982-12-07 Method for desiliconization of molten iron Pending JPS59104414A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21337982A JPS59104414A (en) 1982-12-07 1982-12-07 Method for desiliconization of molten iron

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21337982A JPS59104414A (en) 1982-12-07 1982-12-07 Method for desiliconization of molten iron

Publications (1)

Publication Number Publication Date
JPS59104414A true JPS59104414A (en) 1984-06-16

Family

ID=16638215

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21337982A Pending JPS59104414A (en) 1982-12-07 1982-12-07 Method for desiliconization of molten iron

Country Status (1)

Country Link
JP (1) JPS59104414A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6261339B1 (en) 1998-06-10 2001-07-17 “Holderbank” Financiere Glarus AG Method for desiliconizing pig iron before refining it to steel

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6261339B1 (en) 1998-06-10 2001-07-17 “Holderbank” Financiere Glarus AG Method for desiliconizing pig iron before refining it to steel

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