JPS62205220A - Degassing and desulfurizing method for molten steel - Google Patents

Degassing and desulfurizing method for molten steel

Info

Publication number
JPS62205220A
JPS62205220A JP4519286A JP4519286A JPS62205220A JP S62205220 A JPS62205220 A JP S62205220A JP 4519286 A JP4519286 A JP 4519286A JP 4519286 A JP4519286 A JP 4519286A JP S62205220 A JPS62205220 A JP S62205220A
Authority
JP
Japan
Prior art keywords
molten steel
powder
desulfurizing agent
time
desulfurization
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
Application number
JP4519286A
Other languages
Japanese (ja)
Other versions
JPH0361722B2 (en
Inventor
Noriyuki Shitawara
志俵 教之
Shuhei Onoyama
小野山 修平
Isao Kobayashi
功 小林
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 JP4519286A priority Critical patent/JPS62205220A/en
Publication of JPS62205220A publication Critical patent/JPS62205220A/en
Publication of JPH0361722B2 publication Critical patent/JPH0361722B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To improve desulfurization efficiency and to execute degassing simultaneously by blowing a powder desulfurizing agent to a molten steel upon lapse of the specific time after throwing of Al at the time of blowing the desulfurizing agent into the molten steel in the lower part in a vacuum degassing vessel. CONSTITUTION:Al is added as a deoxidizing agent into the molten steel 3 to decrease the concn. of Al2O3 and in this state, the desulfurizing agent is blown from a tuyere 5 into the molten steel together with a carrier gas 8 via a supply pipe 6 from a desulfurizing agent supplying device 7. The powder desulfurizing agent is blown upon lapse of the t-minute expressed by t=0.02W+5 (t: the time since the throwing of Al until the start of blowing of the powder desulfurizing agent, W: the weight of the molten steel) after throwing of the Al. The desulfurization of the molten steel 3 is thereby executed with high efficiency and at the same time, the degassing is executed as well to desulfurize and degas the molten steel 3 to about <=10ppm S and about <=1.0ppm H.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、RH,DHなどの真空脱ガス装置による溶
鋼の真空脱ガス処理方法に係り特に真空処理槽への粉体
脱硫剤の吹込脱憾剤の吹込方法に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for vacuum degassing treatment of molten steel using a vacuum degassing device such as RH or DH, and particularly relates to a method for degassing molten steel by blowing a powder desulfurization agent into a vacuum treatment tank. This relates to a method of injecting a retardant.

〔従来技術〕[Prior art]

従来の真空処理槽への粉体添加剤送入方法としては、特
公昭45−22204号「溶融金属の真空脱硫方法」が
ある。これはRH真空処理に際して、RHの環流用気体
を添加剤のキャリアーガスとして利用し、上昇管内溶鋼
中へ粉体脱硫剤を懸濁させるものである。しかしながら
、溶鋼中のAl1203  の影響については、言及し
ていない。
A conventional method for feeding powder additives into a vacuum processing tank is disclosed in Japanese Patent Publication No. 45-22204 entitled "Vacuum Desulfurization Method for Molten Metals." This uses the RH reflux gas as a carrier gas for additives during the RH vacuum treatment, and suspends the powder desulfurization agent in the molten steel in the riser pipe. However, no mention is made of the influence of Al1203 in molten steel.

〔発明の解決しようとする問題点〕[Problem to be solved by the invention]

この発明は、従来技術での真空槽内への粉体添加方法に
比べ、M投入による脱酸時から粉体脱硫剤吹込までの時
間をおき、溶鋼中のAl2O3濃度で低減した状態で粉
体脱硫剤ケ吹込むことにより、脱硫効率を飛躍的に向上
させることができると共に脱硫と同時に脱ガスも行なう
ことができ、また真空処理槽の耐火物への影響に最小限
にすることを目的とする。
Compared to the prior art method of adding powder into a vacuum chamber, this invention takes time from the time of deoxidizing by adding M to the time of injecting powder desulfurization agent, and the powder is added in a state where the Al2O3 concentration in the molten steel is reduced. By injecting a desulfurizing agent, desulfurization efficiency can be dramatically improved, and degassing can be performed at the same time as desulfurization, and the purpose is to minimize the impact on the refractories of the vacuum treatment tank. do.

〔問題点の解決手段〕[Means for solving problems]

本発明は以上に述べた従来技術が有する多くの欠点を解
決したもので、真空脱ガス市内下部で且つ溶鋼浴面下に
位置する部分に脱硫剤吹込羽口を設け、その吹込時期イ
、M投入後から A  =  0.02W  +  5 t:AI!、投入後から粉体脱硫剤吹込開始までの時間
(分) W:溶鋼量 で表わされるt分身上経過後、溶鋼中のALz O,s
濃度全低減した状態で、粉体脱硫剤でキャリアーガスに
て溶鋼中に直接吹込むことケ特徴とするものである。
The present invention solves many of the drawbacks of the prior art described above, and includes providing a desulfurizing agent injection tuyere in the lower part of the vacuum degassing city and below the surface of the molten steel bath. After M is turned on, A = 0.02W + 5 t: AI! , time (minutes) from the time of injection until the start of powder desulfurization agent injection W: After t, expressed as the amount of molten steel, ALz O,s in the molten steel
The feature is that the powder desulfurization agent is directly blown into the molten steel using a carrier gas while the concentration is completely reduced.

〔作用〕[Effect]

次に第1図にもとづいて、不発明の1例について詳述す
る。
Next, an example of non-invention will be described in detail based on FIG.

第1図はRH真空槽での例?示めすもので、〕は真空脱
ガス槽、2は排気口、3は溶鋼、4は溶鋼取鍋、5は粉
体脱硫剤吹込羽口、6は粉体脱硫剤供給管、7は脱硫剤
供給装置、8はキャリアーガス体、9はスラグである。
Is Figure 1 an example of an RH vacuum chamber? ] is a vacuum degassing tank, 2 is an exhaust port, 3 is molten steel, 4 is a molten steel ladle, 5 is a powder desulfurization agent injection tuyere, 6 is a powder desulfurization agent supply pipe, and 7 is a desulfurization agent A supply device, 8 is a carrier gas body, and 9 is a slag.

この発明は、溶鋼中のAe20.濃度を低減した状態で
、真望脱ガス処理中に脱硫剤供給装置7から脱硫剤供給
装置6を経由して脱硫剤吹込羽口より溶鋼3中へ脱硫剤
ケ直接吹込むものである。
This invention is directed to Ae20.0 in molten steel. The desulfurizing agent is directly blown into the molten steel 3 from the desulfurizing agent supplying device 7 through the desulfurizing agent supplying device 6 and from the desulfurizing agent injection tuyere during the desired degassing treatment in a reduced concentration state.

Ai!は溶鋼の脱酸剤として添加されるが、このAQ投
入によって生成するAid203は、 粉体脱硫剤と合
体するとサルファイドキャパシティが下がり、脱硫能を
低下させる。したかつで、脱酸剤としてのAC添加と粉
体脱硫剤吹込までの時間ヶ充分おくことにより、溶鋼中
のAl2O3濃度が低減され、粉体脱硫剤との合体が少
なくなり脱硫効率が上がる。
Ai! is added as a deoxidizing agent to molten steel, but when Aid203 produced by adding AQ combines with the powder desulfurizing agent, the sulfide capacity decreases and the desulfurizing ability decreases. By allowing sufficient time between adding AC as a deoxidizing agent and injecting the powder desulfurization agent, the Al2O3 concentration in the molten steel is reduced, the amount of coalescence with the powder desulfurization agent is reduced, and the desulfurization efficiency is increased.

AQ添加から粉体脱硫剤吹込開始までの時間は。What is the time from AQ addition to the start of powder desulfurization agent injection?

長ければ長いほど溶鋼中Aj!203が浮」ニするので
望ましい。が、あまりに長時間となるのは溶製上問題が
あり、またコストの点で得ではない。我々は種々の条件
で操業を行ったネ6来、AQ投入からt ==  0.
02W  +  5 t:A1投入后から粉体脱硫剤吹込開始までの時間(分
) W:溶鋼量、(t) で表わされるt分身上経過後、粉体脱硫剤゛と吹込むこ
とにより脱硫効率が飛躍的に向上することケ見い出した
。第2図に、AC投入後から粉体吹込開始までの時間(
t)と脱硫率の関係で示す。
The longer it is, the more molten steel Aj! 203 is desirable because it floats. However, if the process is too long, there are problems in melting and it is not advantageous in terms of cost. We have conducted operations under various conditions, and since AQ input, t == 0.
02W + 5 t: Time (minutes) from A1 injection to the start of powder desulfurization agent injection W: Molten steel amount, (t) After t has passed, the desulfurization efficiency can be increased by injecting powder desulfurization agent. We found that this improved dramatically. Figure 2 shows the time from turning on the AC to starting powder injection (
t) and the desulfurization rate.

条件 5HでBBでAl 1. OKg/ T投入2)脱硫剤
原単位  3Kq/T 3)処理前(S) ==30〜40 p、pm250T
溶鋼の例であるが、10分以上の時間をおくことにより
10分以下の時間しかおかない場合に比べ脱硫率が安定
して高い。出鋼抜取鍋中で底部からの不活性ガスの吹込
みいわゆるB、 B、の際にM投入しπ例(t=l o
〜12分経過)で、 BBでAg投入の方がRHでAI
全投入しπ例よりわずかに高い脱硫率が得られているが
、これはBBO方がRHに比べ攪拌力が強くA1.20
.濃度の低減が早いためである。
Al in BB under condition 5H 1. OKg/T input 2) Desulfurizing agent consumption 3Kq/T 3) Before treatment (S) ==30~40 p, pm250T
As an example of molten steel, by waiting for 10 minutes or more, the desulfurization rate is stably higher than when waiting for only 10 minutes or less. Inert gas is blown from the bottom of the tapping ladle during so-called B, B, and M is added for π example (t=l o
~12 minutes have elapsed), Ag input at BB is better than AI at RH.
A slightly higher desulfurization rate was obtained than in the π example with full input, but this is because BBO has a stronger stirring force than RH and A1.20
.. This is because the concentration decreases quickly.

また、t=10分経過後の溶鋼を調査した結果、溶鋼中
A12 Os 濃度が約0.O1%以下程度に相当する
もので、Ae2o3#度がこの程度に低くなると粉体脱
硫剤が効率良く脱硫に寄与する。また、150TRHで
は、第2図に示す条件でt、 = 8分以上で脱硫効率
が20%上昇し80係が得られ、溶鋼量が少ない場合に
は5M投入后から、粉体脱硫剤吹込までの時間は少し短
くても高効率となる。
Furthermore, as a result of investigating the molten steel after t=10 minutes, the A12Os concentration in the molten steel was approximately 0. This corresponds to about 1% or less of O, and when the Ae2o3# degree is as low as this, the powder desulfurization agent efficiently contributes to desulfurization. In addition, with 150TRH, under the conditions shown in Figure 2, the desulfurization efficiency increased by 20% to a ratio of 80 at t = 8 minutes or more, and when the amount of molten steel was small, powder desulfurization agent could be injected after 5M was added. Even if the time is a little shorter, the efficiency is high.

まだ、不発明では脱硫効率が飛躍的に向」ニするため、
脱硫剤原単位が低減し、それにつれて耐火物への影響も
少なくすることができる。
However, desulfurization efficiency can be improved dramatically without invention.
The unit consumption of desulfurizing agent is reduced, and the impact on refractories can be reduced accordingly.

〔実施例〕〔Example〕

本発明の実施例として、250T処理槽のF(H真空槽
の実施例ケ示す。
As an example of the present invention, an example of an F(H vacuum chamber) of a 250T processing tank is shown.

実施例] 処理浴鋼量 250T 添加材   All  150 Kg  取鍋へ出鋼後
バブリングVζて冷加 時 間   成投入眉からRH処理開始煮て1(〕分 添加材   (H,C)Fe−Mn  120Kp真空
脱ガス処理開始2分経過後 脱硫剤   80% C,O−20%C,F2キャリア
ーガス(t00N靜/H,Ar処理開始5分経過後 脱硫剤 吹込時間 10分 吹込量  6Kg/T 溶鋼成分変化 実施例2 処理溶鋼量 250T 添加材   Al 150匂出鋼時添加時 間   M
投入後からRH処理開始まで7分 Fe−8i   70Kf 処理開始2分経過後 フラックス 65チ C,0−35チC,F。
Example] Amount of steel in treatment bath 250T Additives All 150 Kg Cooling time by bubbling Vζ after tapping into a ladle RH treatment starts from the end of the steel boiling for 1 minute Additives (H, C) Fe-Mn 120Kp 2 minutes after the start of vacuum degassing treatment, desulfurization agent 80% C, O-20% C, F2 carrier gas (t00N/H, Ar 5 minutes after the start of treatment, desulfurization agent Blow time: 10 minutes Blow rate: 6Kg/T Molten steel composition Variation Example 2 Processing amount of molten steel 250T Additive material Al Addition time for 150 molten steel M
7 minutes from input to start of RH treatment Fe-8i 70Kf 2 minutes after start of treatment Flux 65chi C, 0-35chi C, F.

キャリアーガ、X、 (t100N/H,Ar処理開始
10分経過後 フラックス 吹込時間 10分 吹込量  3匂/T 溶鋼成分変化 上記に示めすように、本発明ではM投入後から粉体脱硫
剤吹込開始までぃ一定の時間をおき、溶鋼中A!2Q、
濃度を低減し、た状態で脱硫することにより脱硫剤の槽
内下部への吹込により(S)≦10ppm、(H)≦1
.oppmを達成している。
Carrier gas, Wait a certain period of time until the start, and during the molten steel A!2Q,
By reducing the concentration and desulfurizing in a state where the desulfurizing agent is blown into the lower part of the tank, (S)≦10ppm, (H)≦1
.. Achieved oppm.

〔発明の効果〕〔Effect of the invention〕

本発明は、M投入から粉体脱懺剤吹込まで、t =  
0.02W  +  5 t:A1投入后から粉体脱硫剤吹込開始までの時間(分
) W:溶鋼量(t) で表わされるt分おき、真空槽内下部から羽口を通して
脱硫剤を直接溶鋼中へ吹込むことにより溶鋼中の〔S〕
≦10 ppm 、 (H)≦1.0ppmという高品
質の鋼を得ることができ脱硫と脱水素の同時処理を可能
とした極めて有用性の高い発明である。
In the present invention, the powder descaling agent is injected from M input, and t =
0.02W + 5 t: Time (minutes) from the time A1 is introduced until the start of powder desulfurization agent injection W: Amount of molten steel (t) Every t minutes, the desulfurization agent is directly injected into the molten steel from the lower part of the vacuum chamber through the tuyere. [S] in molten steel by blowing it into
This is an extremely useful invention that enables the production of high-quality steel of ≦10 ppm and (H)≦1.0 ppm, and enables simultaneous desulfurization and dehydrogenation treatment.

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

第1図は本発明方法に使用する真空脱ガス槽の概要図、
第2図は本発明の効果を示す脱硫率を示す図である。 9:スラグ
Figure 1 is a schematic diagram of the vacuum degassing tank used in the method of the present invention;
FIG. 2 is a diagram showing the desulfurization rate showing the effect of the present invention. 9: Slag

Claims (1)

【特許請求の範囲】 真空脱ガス槽内下部の溶鋼浴面下に設けた脱硫剤吹込羽
口を通して粉体脱硫剤をキャリアーガスにて溶鋼中に直
接吹込むに際し、Al投入後からt=0.02W+5・
・・・・・・・・・・・・・・(分)t:Al投入後か
ら粉体脱硫剤吹込開 始までの時間・・・・・・・(分) w:溶鋼量・・・・・・・・・・・・・(t)で表わさ
れるt分以上経過後、粉体脱硫剤を吹込むことを特徴と
する溶鋼の脱ガス、脱硫方法。
[Claims] When injecting powder desulfurization agent directly into molten steel using a carrier gas through the desulfurization agent injection tuyere provided below the surface of the molten steel bath in the lower part of the vacuum degassing tank, from t=0 after Al is introduced. .02W+5・
・・・・・・・・・・・・・・・(minutes) t: Time from the time of adding Al to the start of powder desulfurization agent injection・・・・・・・・・(minutes) w: Amount of molten steel... A method for degassing and desulfurizing molten steel, characterized by injecting a powder desulfurizing agent after t minutes or more, expressed as (t).
JP4519286A 1986-03-04 1986-03-04 Degassing and desulfurizing method for molten steel Granted JPS62205220A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4519286A JPS62205220A (en) 1986-03-04 1986-03-04 Degassing and desulfurizing method for molten steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4519286A JPS62205220A (en) 1986-03-04 1986-03-04 Degassing and desulfurizing method for molten steel

Publications (2)

Publication Number Publication Date
JPS62205220A true JPS62205220A (en) 1987-09-09
JPH0361722B2 JPH0361722B2 (en) 1991-09-20

Family

ID=12712404

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4519286A Granted JPS62205220A (en) 1986-03-04 1986-03-04 Degassing and desulfurizing method for molten steel

Country Status (1)

Country Link
JP (1) JPS62205220A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000129335A (en) * 1998-10-20 2000-05-09 Nkk Corp Production of extra-low sulfur steel excellent in cleanliness
JP2008260997A (en) * 2007-04-11 2008-10-30 Nippon Steel Corp Desulfurization method of molten steel
JP2016183378A (en) * 2015-03-26 2016-10-20 Jfeスチール株式会社 Desulfurization method for molten steel

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000129335A (en) * 1998-10-20 2000-05-09 Nkk Corp Production of extra-low sulfur steel excellent in cleanliness
JP2008260997A (en) * 2007-04-11 2008-10-30 Nippon Steel Corp Desulfurization method of molten steel
JP2016183378A (en) * 2015-03-26 2016-10-20 Jfeスチール株式会社 Desulfurization method for molten steel

Also Published As

Publication number Publication date
JPH0361722B2 (en) 1991-09-20

Similar Documents

Publication Publication Date Title
JPS62205220A (en) Degassing and desulfurizing method for molten steel
JPH09157732A (en) Method for desulfurizing and dehydrogenating molten steel with little erosion of refractory
JPS61253312A (en) Purification of molten metal bath regulating nitrogen
US5897684A (en) Basic oxygen process with iron oxide pellet addition
KR100270109B1 (en) The denitriding method of molten metal
JPH0153329B2 (en)
JPH0987732A (en) Method for refining molten steel
JP3233304B2 (en) Production of low Si, low S, and high Mn hot metal with smelting reduction of Mn ore
JPH0873923A (en) Production of clean steel having excellent hydrogen induced crack resistance
KR100336855B1 (en) Flux wire for use in the manufacture of high purity aluminum deoxidized steel
JP4096632B2 (en) Desulfurization method of molten steel under reduced pressure
JP3508550B2 (en) Hot metal desulfurization method
RU2096491C1 (en) Steel foundry process
JPS636606B2 (en)
KR940008457B1 (en) Desulfurising method
JPH0361725B2 (en)
JPS6124450B2 (en)
JP3800866B2 (en) Hot metal desiliconization method
RU2228373C1 (en) Method of refining low-silicon steel in ladle
JPS6396210A (en) Pre-deoxidizing method in converter interior
RU2171296C1 (en) Method of steel treatment
JPH1088216A (en) Method for desulfurizing molten iron
JPH02200715A (en) Method for dephosphorizing and desulfurizing molten iron
SU929713A1 (en) Method for treating molten steel
SU765367A1 (en) Method of out-of-blast furnace treatment of molten cast iron

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term