JPS58221210A - Preliminary treatment of molten iron - Google Patents

Preliminary treatment of molten iron

Info

Publication number
JPS58221210A
JPS58221210A JP10192682A JP10192682A JPS58221210A JP S58221210 A JPS58221210 A JP S58221210A JP 10192682 A JP10192682 A JP 10192682A JP 10192682 A JP10192682 A JP 10192682A JP S58221210 A JPS58221210 A JP S58221210A
Authority
JP
Japan
Prior art keywords
hot metal
lance
pipe
molten iron
gas
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
JP10192682A
Other languages
Japanese (ja)
Inventor
Tsutomu Nozaki
野崎 努
Michiharu Ozawa
小沢 三千晴
Hideji Takeuchi
秀次 竹内
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
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP10192682A priority Critical patent/JPS58221210A/en
Publication of JPS58221210A publication Critical patent/JPS58221210A/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

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 compensate the decrease in the carbon content in molten iron by immersing a lance of double-pipe construction into the molten iron, blowing a treating agent for molten iron through the inside pipe and blowing gaseous hydrocarbon through the flow passage between the inside and outside pipes thereby preventing the erosion at the forward end of the lance. CONSTITUTION:A lance 8 of the double-pipe construction consisting of an inside pipe 1 and an outside pipe 2 is immersed in the molten iron 10 in a preliminary treatment vessel 9. A treating agent 11 for molten iron is supplied into the flow passage 3 of the inside pipe 1 of the lance 8 by using a carrier gas 12 and is blown into the iron 10 through an inside blow port 5. At the same instant, gaseous hydrocarbon 13 is supplied into the outside flow passage 4 formed between the pipe 1 and the pipe 2 of the lance 8 and is blown into the iron 10 through an outside blow port 6, whereby the molten iron is subjected to preliminary treatments such as desiliconization, dephosphorization and desulfurization. The erosion at the forward end of the lance 8 is prevented by the above-mentioned method; in addition, the content of the carbon in the molten iron decreased in the decarburization treatment is compensated and the heat source for refining in a converter, etc. is assured.

Description

【発明の詳細な説明】 この発明は転炉等における脱炭精錬に先立って溶銑の脱
珪、脱燐、脱硫のために行なわれる溶銑予備処理法に関
し、特に溶銑中に浸漬させたランスを介して予備処理剤
を溶銑中に吹込むように閾所謂インジエクシ冒ン方式に
よる溶銑予備処理方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a hot metal pretreatment method that is carried out for desiliconization, dephosphorization, and desulfurization of hot metal prior to decarburization refining in a converter, etc. The present invention relates to a hot metal pretreatment method using a so-called in-die injection method in which a pretreatment agent is blown into the hot metal.

周知のように溶銑予備処理は、転炉等における精錬に先
立って脱珪、脱燐、脱硫を行ない、これにより続く転炉
等の精錬における負荷を減少させ、製鋼過程の高能率化
や鉄歩留りの向上、製鋼副原料原単位の削減等を図るこ
とを目的としている。
As is well-known, hot metal pretreatment involves desiliconization, dephosphorization, and desulfurization prior to refining in a converter, etc., which reduces the load on subsequent refining in a converter, etc., and improves the efficiency of the steelmaking process and improves iron yield. The aim is to improve the production efficiency and reduce the basic unit of steelmaking auxiliary raw materials.

このような溶銑予備処理に使用されている処理剤は炭酸
ソーダ(Na2co3)系のものと、生石灰(CaO)
系のものとに大別されるが、いずれの処理剤においても
処理効率、特に脱燐効率を向上させるためには、処理剤
の粉体が溶銑中を浮上する過程を有効に利用することが
望ましく、そこで最近では処理剤粉体を溶銑中に吹込む
所謂インジェクション方式が種々開発・実用化されるに
至っている。
The processing agents used for hot metal pretreatment are soda carbonate (Na2co3) and quicklime (CaO).
In order to improve treatment efficiency, especially dephosphorization efficiency, for any type of treatment agent, it is necessary to effectively utilize the process in which the powder of the treatment agent floats through the hot metal. Therefore, recently, various so-called injection methods, in which processing agent powder is injected into hot metal, have been developed and put into practical use.

しかるに上述のようなインジェクション方式による溶銑
予備処理には次のような種々の問題があった。すなわち
、インジェクション方式による溶銑予備処理においては
、ランスを溶銑中に浸漬させ、窒素ガスあるいは酸素ガ
ス、または両者の混合ガスを搬送ガスとして前記ランス
を介して予備処理剤を溶銑中に吹込むのが通常である。
However, the hot metal pretreatment using the injection method as described above has the following various problems. That is, in hot metal pretreatment by the injection method, a lance is immersed in the hot metal, and a pretreatment agent is injected into the hot metal through the lance using nitrogen gas, oxygen gas, or a mixture of both as a carrier gas. Normal.

ここで脱燐反応は酸化反応であるから、脱燐効率を良好
にする庭めには搬送ガスとして酸素ガス混合割合の高い
混合ガス、あるいは純酸素ガスを使用することが望まし
いと考えられる。しかしながら酸素ガス混合割合を高く
した場合や純酸素ガスを使用した場合には、それらの酸
化性ガスと溶銑中の各種成分との発熱反応によってラン
ス先端部附近が高温となってランス先端の溶損が激しく
なり、その結果、予備処理中途において処理剤粉体の吹
込みを中断しなければならない事態がしばしば発生する
。また搬送ガスとして酸素ガス混合割合の高い混合ガス
や純酸素ガスを用いた場合、溶銑中の燐、珪素、硫黄の
みならず炭素も相当量が酸化除、去されてしまい、溶銑
炭素濃度が低下してしまう3溶銑中の炭素は続く転炉吹
錬における熱源であるから、上述のように溶銑予備処理
において溶銑中炭素濃度が低下してしまえば、転炉吹錬
工程において熱源が不足し、鋼浴温度を所定の目標温度
に確保することが困難となる問題が生じる。さらに溶銑
の脱硫反応においては酸素分圧P 02が低い方が有利
であることが知られているが、前述のように酸素混合割
合の高い混合ガスや純酸素ガスを用いればP O2が高
くなって脱硫反応に著しく不利となり、脱硫率が低下す
る問題がある。
Here, since the dephosphorization reaction is an oxidation reaction, it is considered desirable to use a mixed gas with a high oxygen gas mixing ratio or pure oxygen gas as the carrier gas in order to improve the dephosphorization efficiency. However, when the oxygen gas mixing ratio is increased or when pure oxygen gas is used, the area around the lance tip becomes high temperature due to the exothermic reaction between these oxidizing gases and various components in the hot metal, leading to melting of the lance tip. As a result, it is often necessary to interrupt the injection of the processing agent powder in the middle of the pretreatment. Furthermore, when a mixed gas with a high oxygen gas mixing ratio or pure oxygen gas is used as a carrier gas, not only phosphorus, silicon, and sulfur in the hot metal but also a considerable amount of carbon are oxidized and removed, resulting in a decrease in the hot metal carbon concentration. 3. Carbon in the hot metal is a heat source in the subsequent converter blowing, so if the carbon concentration in the hot metal decreases in the hot metal pretreatment as described above, there will be a shortage of heat source in the converter blowing process, A problem arises in that it is difficult to maintain the steel bath temperature at a predetermined target temperature. Furthermore, in the desulfurization reaction of hot metal, it is known that a lower oxygen partial pressure P02 is more advantageous; however, as mentioned above, if a mixed gas with a high oxygen mixing ratio or pure oxygen gas is used, the P02 will be higher. There is a problem that this becomes extremely disadvantageous for the desulfurization reaction and the desulfurization rate decreases.

以上のように従来のインジエクシlン方式による溶銑予
備処理においては、脱燐効率を高くするために搬送ガス
として酸素ガス混合割合の高い混合ガスもしくは純酸素
ガスを用いた場合、(1)ランスの溶損、(2)溶銑中
炭素濃度の低下に起因する転炉吹錬の困難さ、(3)脱
硫率の低下、などの問題を招く欠点があった。
As mentioned above, in hot metal pretreatment using the conventional Indie Excine method, when a mixed gas with a high oxygen gas mixing ratio or pure oxygen gas is used as the carrier gas in order to increase the dephosphorization efficiency, (1) the lance There were drawbacks such as melting loss, (2) difficulty in converter blowing due to a decrease in carbon concentration in hot metal, and (3) decrease in desulfurization rate.

この発明は以上の事情に鑑みてなされたもので、溶銑処
理剤の搬送ガスとして酸素ガス混合割合の高い混合ガス
や純酸素ガスを用いた場合でも、ランスの溶損が可及的
に防止されるようにするとともに、転炉吹錬時において
熱源となる溶銑中炭素の減少を補償し、併せて脱硫率の
低下が防止されるようにすることを目的とするものであ
る。
This invention was made in view of the above circumstances, and even when a mixed gas with a high oxygen gas mixing ratio or pure oxygen gas is used as the carrier gas for the hot metal treatment agent, it is possible to prevent lance erosion as much as possible. The purpose of this invention is to compensate for the decrease in carbon in hot metal, which is a heat source during converter blowing, and to prevent a decrease in the desulfurization rate.

すなわちこの発明の溶銑予備処理方法は、溶銑処理剤を
吹込むだめのランスを2重管構造とし、その内管から処
理剤を吹込むと同時に、内管と外管との間の流路から炭
化水素系ガスを吹込むことを特徴とするものである。
That is, in the hot metal pretreatment method of the present invention, the lance for injecting the hot metal treatment agent has a double tube structure, and at the same time, the treatment agent is injected from the inner tube and from the flow path between the inner tube and the outer tube. It is characterized by blowing in hydrocarbon gas.

以下この発明の溶銑予備処理法についてさらに詳細に説
明する。
The hot metal pretreatment method of the present invention will be explained in more detail below.

この発明の方法では上述のように溶銑中に浸漬させて溶
銑処理剤を吹込むだめのランスとして、2重管構造のも
のを用いる。具体的には例えば第1図に示すようにステ
ンレス鋼、普通鋼等からなるストレートな内管1の外側
を、間隔を置いて同心状に同様な材質からなる外管2に
よって取囲み、内管1の内側の流路3と、内管1と外管
2との間の流路4との両者に各別に流体を流し得るよう
に構成し、かつ台管1,2の下方開口端をそれぞれ内側
吹出口5、外側吹出口6とし、さらに外管2の外周面に
耐火物7を設けたランスを用いれば良い。あるいはまた
第2図もしくは第3図に示すように、内管1の下端を逆
T字状もしくは逆T字状に分岐させ、内側吹出口5およ
び外側吹出口6を(5) それぞれ左右一対形成し九ランスを用いても良い。
In the method of this invention, as described above, a double-pipe lance is used as the lance that is immersed in the hot metal and into which the hot metal treatment agent is blown. Specifically, as shown in FIG. 1, for example, the outside of a straight inner tube 1 made of stainless steel, ordinary steel, etc. is surrounded by outer tubes 2 made of the same material concentrically at intervals, and the inner tube 1 and the flow path 4 between the inner tube 1 and the outer tube 2. A lance having an inner outlet 5 and an outer outlet 6 and a refractory 7 provided on the outer circumferential surface of the outer tube 2 may be used. Alternatively, as shown in FIG. 2 or 3, the lower end of the inner tube 1 is branched into an inverted T-shape or an inverted T-shape to form a left and right pair of inner air outlet 5 and outer air outlet 6 (5). You may also use a shiku lance.

この発明の溶銑予備処理法においては、上述のような2
重管構造のランス8の下部を溶銑装入鍋あるいは混銑車
等の予備処理容器9内の溶銑10中に浸漬させ、前記ラ
ンス8の内管1内の流路に溶銑処理剤11を窒素ガス、
もしくは酸素ガス、ま九はこれらの混合ガスからなる搬
送ガス12を用いて供給し、その先端の内側吹込口から
溶銑中に溶銑処理剤11を前記搬送ガス12とともに吹
込み、同時にランス8の外側流路に炭化水素系ガス(C
nHm)13を供給し、その先端の外側吹込[コから溶
銑中に炭化水素系ガス13を吹込む。
In the hot metal pretreatment method of this invention, the above-mentioned two
The lower part of the lance 8 having a heavy pipe structure is immersed in hot metal 10 in a pre-treatment container 9 such as a hot metal charging pot or a pig iron mixing car, and a hot metal treatment agent 11 is introduced into the flow path in the inner pipe 1 of the lance 8 using nitrogen gas. ,
Alternatively, oxygen gas is supplied using a carrier gas 12 made of a mixture of these gases, and the hot metal treatment agent 11 is blown into the hot metal together with the carrier gas 12 from the inner blowing port at the tip, and at the same time the outer side of the lance 8 is Hydrocarbon gas (C
nHm) 13 is supplied, and the hydrocarbon gas 13 is blown into the hot metal from the outside blowing point at the tip.

前記溶銑処理剤としては、従来から知られているような
生石灰系フラックスまたは炭酸ソーダ系スラックスを用
いれば良い。すなわち生石灰系7ラツクスとしては、生
石灰(CaO)を主成分としこれに鉄鉱石やミルスケー
ル等の酸化鉄を混合したフラックス、あるいはこれらに
媒溶剤としてのCa F 2等のフッ化物、CaC−9
2等の塩化物、Na2CO3等のアルカリ金属の炭酸塩
のうちから選ばれた1(6) 種または2種以上のものを混合したフラックスが用いら
れる。また炭酸ソーダ系フラックスとしては、炭酸ソー
ダ(Na2C03)を主成分としこれに必要に応じて鉄
鉱石等の酸化鉄を加えたフラックスが用いられる。また
その溶銑処理剤を吹込むだめの搬送ガスとしては、前述
したように脱燐効率を高めるためKは酸素ガス混合比率
が高い酸素−窒素混合ガス(例えば0260%以上)、
または純酸素ガスを使用することが望ましく、かつその
場合にこの発明の効果が最も期待できるが、必ずしもそ
れに限らず、酸素ガス混合比率が低い混合ガスや窒素ガ
スを搬送ガスとする場合にも適用可能である。
As the hot metal treatment agent, a conventionally known quicklime-based flux or soda carbonate-based flux may be used. In other words, quicklime-based 7-luxes include fluxes whose main component is quicklime (CaO) mixed with iron oxides such as iron ore and mill scale, or fluxes containing fluorides such as CaF2 and CaC-9 as solvents.
The flux used is one (6) selected from chlorides such as No. 2, carbonates of alkali metals such as Na2CO3, or a mixture of two or more of them. As the soda carbonate flux, a flux containing soda carbonate (Na2C03) as a main component and iron oxide such as iron ore added thereto as necessary is used. In addition, as the carrier gas for blowing the hot metal treatment agent, K is an oxygen-nitrogen mixed gas with a high oxygen gas mixing ratio (for example, 0.260% or more) in order to increase the dephosphorization efficiency, as described above.
Alternatively, it is preferable to use pure oxygen gas, and in that case, the effects of the present invention can be expected most, but it is not necessarily limited to this, and can also be applied when a mixed gas with a low oxygen gas mixing ratio or nitrogen gas is used as the carrier gas. It is possible.

一方外側流路に流す炭化水素系ガスとしてはプロパy 
(C3HB )、ブタン(C4H10)が代表的であり
、またこの他天然ガスも使用できる。
On the other hand, the hydrocarbon gas flowing into the outer flow path is propylene gas.
(C3HB) and butane (C4H10) are typical, and natural gas can also be used.

上述のようにランスの外側流路に流す炭化水素系ガスは
、溶銑中に吹込まれて高温で分解するが、その分解反応
は吸熱反応であるから、ランス先端附近の熱を奪う。し
たがって内管から吹込む溶銑処理剤の搬送ガスが酸素ガ
スあるいは酸素濃度の高い混合ガスであっても、ランス
先端の発熱による溶損が有効に防止される。
As mentioned above, the hydrocarbon gas flowing through the outer flow path of the lance is blown into the hot metal and decomposed at high temperature, but since the decomposition reaction is an endothermic reaction, it takes away the heat near the tip of the lance. Therefore, even if the carrier gas for the hot metal treatment agent blown in from the inner tube is oxygen gas or a mixed gas with a high oxygen concentration, melting damage due to heat generation at the tip of the lance can be effectively prevented.

また炭化水素系ガス(CH)の1モルが分解すればnモ
ルの炭素(C)が生じて溶銑中に溶解されるから、溶銑
予備処理に引続く転炉吹錬に必要なC量の脱炭による不
足分を補うことができ、その結果転炉吹錬時における目
標温度を支障なく確保することが可能となる。
In addition, when 1 mole of hydrocarbon gas (CH) is decomposed, n moles of carbon (C) are generated and dissolved in the hot metal, so the amount of carbon required for converter blowing following hot metal pretreatment is eliminated. The shortage of charcoal can be compensated for, and as a result, it becomes possible to secure the target temperature during converter blowing without any problem.

さらに、炭化水素系ガス(CnHm)の1モルの分解に
よって1モルの水素ガスが発生する。通常はmの値は8
以上であるから、4モル程度以上の水素ガスが発生し、
そのため雰囲気の一酸化炭素分圧PCOが低下し、併せ
て酸素分圧P。も低下するから、脱硫効率も向上するこ
とになる。
Furthermore, 1 mol of hydrogen gas is generated by decomposing 1 mol of hydrocarbon gas (CnHm). Usually the value of m is 8
Because of the above, hydrogen gas of about 4 moles or more is generated,
Therefore, the atmospheric carbon monoxide partial pressure PCO decreases, and the oxygen partial pressure P also decreases. Since the desulfurization efficiency also decreases, the desulfurization efficiency also improves.

次にこの発明の実施例および従来法による比較例を記す
Next, examples of the present invention and comparative examples using a conventional method will be described.

実施例 溶銑装入鍋もしくは混銑車内の溶銑100トンに対して
2重管構造のランスを用いて吹込み実験を行った。ラン
スの内管および外管の材質は普通鋼とし、内管の内径は
3Q+am、内管と外管との隙間は1mとした。溶銑処
理剤としては公知のCaO系フラックス(Ca030 
%、鉄鉱石60%、Ca F 210%)を用い、これ
を窒素ガスと酸素ガスとの混合比1:4の混合ガスによ
って内管から381rtインジエクシヨンすると同時に
外管と内管との間の隙間からプロパンガスを吹込んだ。
EXAMPLE A blowing experiment was carried out on 100 tons of hot metal in a hot metal charging pot or a hot metal mixing car using a double pipe lance. The material of the inner and outer tubes of the lance was ordinary steel, the inner diameter of the inner tube was 3Q+am, and the gap between the inner tube and the outer tube was 1 m. As a hot metal treatment agent, known CaO-based flux (Ca030
%, iron ore 60%, Ca F 210%), this was injected at 381 rt from the inner tube with a mixed gas of nitrogen gas and oxygen gas at a mixing ratio of 1:4, and at the same time the gap between the outer tube and the inner tube was Propane gas was blown in.

但し内管の混合ガス流量は5 N771%in 、外側
のプロパンガス流量は0.25 Nmyminとした。
However, the mixed gas flow rate in the inner tube was 5 N771%in, and the propane gas flow rate in the outer tube was 0.25 Nmymin.

比較例 前記実施例と同様に100トンの溶銑に対して、単管構
造のランスを用いて吹込み実験を行った。
Comparative Example As in the previous example, a blowing experiment was carried out on 100 tons of hot metal using a single tube lance.

ランスの管材質は普通鋼、その内径は3o−とし、また
溶銑処理剤としては前記同様なCaO系フラックスを用
い、これを前記と同じ混合ガスを搬送ガスとしてほぼ同
量吹込んだ◎ 以上の実施例および比較例における溶銑の処理前後の成
分、温度、処理中における溶銑中炭素量の減少量(ΔC
)、およびランス耐用ヒート数を第1表に示す。
The pipe material of the lance was ordinary steel, its inner diameter was 3o-, and the same CaO-based flux as above was used as the hot metal treatment agent, and approximately the same amount of the same mixed gas as above was injected as the carrier gas.◎ In Examples and Comparative Examples, the components of hot metal before and after treatment, the temperature, and the amount of decrease in the amount of carbon in hot metal during treatment (ΔC
), and the number of heats the lance can withstand are shown in Table 1.

(9) 第1表から明らかなように単管構造のランスを用いた従
来法による比較例においては1本のランスの耐用回数が
3〜4回であったのに対し、この発明の実施例において
はランス先端の溶損が少ないため約2倍の耐用回数が得
られた。また従来法による比較例においては0.5%程
度の脱炭(溶銑中炭素量減少)が認められ、引続く転炉
吹錬における目標温度確保困難となったのに対し、この
発明の実施例では溶銑中炭素減少量が0,1チ以内に抑
えられ、その結果引続く転炉吹錬における目標温度確保
が容易となった。さらに脱硫率についてもこの発明の実
施例の場合には従来法による比較例と比べて良好となる
ことが確認された。
(9) As is clear from Table 1, in the comparative example using the conventional method using a lance with a single tube structure, the durability of one lance was 3 to 4 times, whereas in the example of the present invention Because there was less erosion at the tip of the lance, the service life was approximately twice as long. In addition, in the comparative example using the conventional method, decarburization (reduction in the amount of carbon in the hot metal) of about 0.5% was observed, making it difficult to maintain the target temperature in the subsequent converter blowing, whereas the example of the present invention In this case, the amount of carbon reduction in the hot metal was suppressed to within 0.1 inch, and as a result, it became easy to secure the target temperature in the subsequent converter blowing. Furthermore, it was confirmed that the desulfurization rate was better in the examples of the present invention than in the comparative examples using the conventional method.

以上のようにこの発明の溶銑予備処理方法によれば、ラ
ンス先端の溶損を防止することができ、かつまた処理中
の脱炭による溶銑中炭素量減少を補償して、引続く転炉
等における精錬での熱源を確保することにより鋼浴の目
標温度を容易に確保することができ、さらには脱硫率の
低下を防止できる等、種々の効果が得られる。
As described above, according to the hot metal pretreatment method of the present invention, it is possible to prevent the melting loss of the tip of the lance, and also compensate for the decrease in the amount of carbon in the hot metal due to decarburization during treatment, so that the subsequent converter etc. By securing a heat source for the refining process, it is possible to easily maintain the target temperature of the steel bath, and furthermore, a variety of effects can be obtained, such as being able to prevent a decrease in the desulfurization rate.

(II) (10)(II) (10)

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

第1図から第3図まではそれぞれこの発明の溶銑予備処
理方法に使用される2重管構造のランスの一例を示す断
面図、第4図はこの発明の溶銑予備処理方法を実施して
いる状況の一例を示す略解図である。 1・・・内管、3・・・外管、4・・・内管と外管との
間の流路、7・・・耐火物、8・・・ランス、10・・
・溶銑、11・・・溶銑処理剤、12・・・窒素ガスお
よび/または酸素ガスからなる搬送ガス、13・・・炭
化水素系ガス。 出願人 川崎製鉄株式会社 (12) 第1図  第2図  第3図 第4図 53−
Figures 1 to 3 are cross-sectional views showing an example of a double-pipe structure lance used in the hot metal pretreatment method of the present invention, and Figure 4 shows a diagram in which the hot metal pretreatment method of the present invention is implemented. It is a schematic diagram showing an example of the situation. DESCRIPTION OF SYMBOLS 1... Inner tube, 3... Outer tube, 4... Channel between inner tube and outer tube, 7... Refractory, 8... Lance, 10...
-Hot metal, 11...Hot metal treatment agent, 12...Carrier gas consisting of nitrogen gas and/or oxygen gas, 13...Hydrocarbon gas. Applicant: Kawasaki Steel Corporation (12) Figure 1 Figure 2 Figure 3 Figure 4 53-

Claims (1)

【特許請求の範囲】 転炉等における脱炭精錬に先立ち、溶銑中にう/スを浸
漬させてそのランスを介して溶銑処理剤を溶銑中に吹込
んで溶銑を予備処理する方法において、 前記ランスを2重管構造とし、そのランスの内管から窒
素ガスおよび/または酸素ガスを搬送ガスとして溶銑処
理剤を溶銑中に吹込むと同時に、内管と外管との間の流
路から炭化水素系ガスを溶銑中に吹込むことを特徴とす
る溶銑予備処理方法。
[Scope of Claims] A method of pre-treating hot metal by immersing a waste in hot metal and injecting a hot metal treatment agent into the hot metal through the lance, prior to decarburization refining in a converter or the like, comprising: The lance has a double pipe structure, and the hot metal treatment agent is blown into the hot metal from the inner pipe of the lance using nitrogen gas and/or oxygen gas as a carrier gas, and at the same time, hydrocarbons are injected from the flow path between the inner pipe and the outer pipe. A hot metal pretreatment method characterized by blowing system gas into hot metal.
JP10192682A 1982-06-14 1982-06-14 Preliminary treatment of molten iron Pending JPS58221210A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10192682A JPS58221210A (en) 1982-06-14 1982-06-14 Preliminary treatment of molten iron

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10192682A JPS58221210A (en) 1982-06-14 1982-06-14 Preliminary treatment of molten iron

Publications (1)

Publication Number Publication Date
JPS58221210A true JPS58221210A (en) 1983-12-22

Family

ID=14313514

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10192682A Pending JPS58221210A (en) 1982-06-14 1982-06-14 Preliminary treatment of molten iron

Country Status (1)

Country Link
JP (1) JPS58221210A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007254889A (en) * 2006-02-27 2007-10-04 Jfe Steel Kk Oxygen gas blowing-lance for refining, and method for desiliconize-treatment of molten iron
JP2008266674A (en) * 2007-04-17 2008-11-06 Jfe Steel Kk Method for desiliconizing molten pig iron
JP2009084670A (en) * 2007-10-03 2009-04-23 Jfe Steel Kk Oxygen gas blowing lance and molten iron desiliconization method
JP2010095740A (en) * 2008-10-15 2010-04-30 Jfe Steel Corp Method for desiliconizing molten pig iron

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007254889A (en) * 2006-02-27 2007-10-04 Jfe Steel Kk Oxygen gas blowing-lance for refining, and method for desiliconize-treatment of molten iron
JP2008266674A (en) * 2007-04-17 2008-11-06 Jfe Steel Kk Method for desiliconizing molten pig iron
JP2009084670A (en) * 2007-10-03 2009-04-23 Jfe Steel Kk Oxygen gas blowing lance and molten iron desiliconization method
JP2010095740A (en) * 2008-10-15 2010-04-30 Jfe Steel Corp Method for desiliconizing molten pig iron

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