JPS6191311A - Refining method of molten steel - Google Patents

Refining method of molten steel

Info

Publication number
JPS6191311A
JPS6191311A JP59213330A JP21333084A JPS6191311A JP S6191311 A JPS6191311 A JP S6191311A JP 59213330 A JP59213330 A JP 59213330A JP 21333084 A JP21333084 A JP 21333084A JP S6191311 A JPS6191311 A JP S6191311A
Authority
JP
Japan
Prior art keywords
molten steel
steel
molten
slag
deoxidation
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
JP59213330A
Other languages
Japanese (ja)
Inventor
Hirohisa Nakajima
中島 廣久
Yoshimi Komatsu
喜美 小松
Masabumi Ikeda
正文 池田
Tsuneo Kondo
恒雄 近藤
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 Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP59213330A priority Critical patent/JPS6191311A/en
Priority to US06/782,527 priority patent/US4652308A/en
Priority to DE8585112614T priority patent/DE3581475D1/en
Priority to EP85112614A priority patent/EP0179337B1/en
Priority to ZA857708A priority patent/ZA857708B/en
Priority to KR1019850007459A priority patent/KR900002574B1/en
Priority to CA000492824A priority patent/CA1244245A/en
Publication of JPS6191311A publication Critical patent/JPS6191311A/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
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/0075Treating in a ladle furnace, e.g. up-/reheating of molten steel within the ladle

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Steel In Its Molten State (AREA)

Abstract

PURPOSE:To produce a steel contg. N2 at a lower rate at a good yield of a deoxidizing agent by putting the molten steel tapped from a converter without deoxidation into a ladle refining furnace and adding the deoxidizing agent such as Al to the molten steel after removing molten slag therefrom. CONSTITUTION:The pickup of N2 from the inside of the air increases if the content of O2 in the molten steel is low. The molten steel tapped from the converter is therefore tapped together with the molten slag into the ladle refining furnace without subjecting the same to the deoxidizing treatment. Al as the deoxidizing agent is added to the molten steel after the molten slag is removed in the ladle refining furnace. The Al is used for the deoxidation of the molten steel at a high yield without oxidation loss by the molten slag as molten slag does not exist in the molten steel. The pickup of N2 is eliminated as the molten steel is not deoxidized in the stage of tapping from the converter. The deoxidation with high yield of the Al which is the reducing agent is thus made possible and the low nitrogen steel is produced stably at a low cost.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、取鍋精錬炉を用σ)だ溶鋼の溶製方法とくに
低窒素鋼の溶製方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing molten steel using a ladle refining furnace, particularly a method for producing low nitrogen steel.

〔従来の技術〕[Conventional technology]

一般に溶鋼の溶製は、転炉で吹錬した後取鍋に出鋼して
おこなうが、出鋼時にその温度を1630〜40℃前後
として温度補償を行ない。
Generally, molten steel is produced by blowing it in a converter and then tapping it into a ladle, but at the time of tapping, the temperature is set at around 1630 to 40° C. and temperature compensation is performed.

更に出鋼時に脱酸剤1合金鉄を添加して既脱酸出鋼を行
なっている。モして取鍋内ではスラグなそのままの状態
として、バブリング等を行っている。
Furthermore, deoxidized steel is produced by adding deoxidizer 1 ferroalloy at the time of steel tapping. The slag remains in the ladle and is bubbled.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

一般に溶鋼中のO3の景によってN、の吸着能が異なり
、0.の量が少なくなると吸着能が高くなることが知ら
れている。従来方法では、出鋼時に脱酸するため、N2
の巻き込みやいわゆるピックアップが生じ、溶鋼中のN
、含有量が増加してしまう。
In general, the adsorption capacity of N varies depending on the O3 content in molten steel, and 0. It is known that the adsorption capacity increases as the amount of . In the conventional method, N2 is used to deoxidize during tapping.
This causes the N in the molten steel to become entangled or to be picked up.
, the content will increase.

しかも脱酸剤であるAlを添加しても、その一部がスラ
グと反応して、脱酸に寄与せず、A!添加量が必要以上
に多い。またスラグと反応するAltのバラツキが多く
、一定量のAlを添加しても脱酸量が変動し、所望の脱
酸を行なうことが困難である。
Moreover, even if Al, which is a deoxidizing agent, is added, a part of it reacts with the slag and does not contribute to deoxidizing.A! The amount added is larger than necessary. Furthermore, there is a large variation in Alt reacting with slag, and even if a certain amount of Al is added, the amount of deoxidation varies, making it difficult to perform desired deoxidation.

本発明は、上記事情に鑑みてなされたもので、その目的
とするところは、とくに低窒素鋼を安定して得ることが
でき、しかもへ!添加量が少なく、かつ安定している溶
鋼の溶製方法な得んとするものである。
The present invention has been made in view of the above circumstances, and its purpose is to be able to stably obtain low-nitrogen steel, and moreover! This is an advantageous method for producing molten steel in which the amount of addition is small and is stable.

〔発明の構成〕[Structure of the invention]

本発明は、転炉から未脱酸出鋼してN、の巻き込み、ピ
ックアップを防止した後、取鍋精錬炉でスラグを除去し
てから脱酸剤を添加することによ:)、スラグの影響を
受けずに少量かつ安定して脱酸を行なえかつ狭範囲のS
。A−Alコントロール(0,0151幅)が可能とな
るようにした溶鋼の精錬方法である。
In the present invention, after extracting undeoxidized steel from a converter and preventing the entrainment and pickup of N, the slag is removed in a ladle refining furnace and then a deoxidizing agent is added. Able to stably deoxidize in small quantities without being affected and with a narrow range of S.
. This is a molten steel refining method that enables A-Al control (0.0151 width).

以下本発明の詳細な説明する。The present invention will be explained in detail below.

本発即では、まず転炉から未脱酸出鋼する。In the first stage of production, undeoxidized steel is tapped from the converter.

従来のように出鋼時に脱酸すると窒素が為き込まれやす
く、またピックアップがおこるが1本発明の如く未脱酸
出鋼すると窒素の巻き込み、ピックアップを防止し、そ
の結果溶鋼中の窒素含有量を少なくすることができる。
If deoxidized at the time of tapping as in the past, nitrogen tends to be drawn in and pick-up occurs, but if the steel is tapped without being deoxidized as in the present invention, the entrainment and pickup of nitrogen is prevented, and as a result, the nitrogen content in the molten steel is reduced. The amount can be reduced.

次いで取鍋精錬炉でスラグを除去してから脱酸剤を添加
する。スラグを除去しであるので、脱酸剤であるAAが
スラグと反応することがなく、A!添加量を必要最小限
とすることができる。また八!がスラグの影響を受けな
いので安定して脱酸を行うことができ、所定のAI添加
量で所望の脱酸を行ない、かつ狭範囲の5ob−AAコ
ントロール(0,015チ)が可能である。この場合、
スラグの除去方法は、常法によっておこない、例えば真
空吸着処理(VSC)により除去するのが好適である。
The slag is then removed in a ladle refining furnace and a deoxidizing agent is added. Since the slag is removed, the deoxidizing agent AA does not react with the slag, and A! The amount added can be kept to the minimum necessary. See you again! Since it is not affected by slag, deoxidation can be performed stably, desired deoxidation can be performed with a predetermined amount of AI added, and narrow range 5ob-AA control (0,015chi) is possible. . in this case,
The slag is preferably removed by a conventional method, for example, by vacuum suction treatment (VSC).

〔実施例〕〔Example〕

普通銑を未脱酸出鋼しく出鋼温度+63o’C)、真空
吸着処理でスラグを除去した後、取鍋精錬炉にAAを1
.20 Kl”ントン添加して脱酸した。
After removing the slag from undeoxidized ordinary pig (extraction temperature +63o'C) and vacuum adsorption treatment, 1 AA was added to the ladle refining furnace.
.. 20 Klton was added to deoxidize.

得られた素鋼の窒素含有量は15〜20 pI)m、で
あった。
The nitrogen content of the obtained raw steel was 15 to 20 pI)m.

これに対し、従来方法で出鋼時にAAを1.55Kp/
)ン添加して既脱酸出鋼したものは、素鋼の窒素含有量
が20〜a o p’p mであった。
On the other hand, in the conventional method, AA is 1.55Kp/
) The nitrogen content of the raw steel was 20 to ao p'pm.

このことから実施例のものは窒素含有量を少なくでき、
又%A!AA量も少なくできることがわかる。また実施
例のものは、酸素含有量のバラツキが従来法に比べて少
ないことがわかる。
From this, the nitrogen content of the example can be reduced,
Also %A! It can be seen that the amount of AA can also be reduced. Furthermore, it can be seen that the variations in oxygen content in the examples are smaller than in the conventional method.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明によれば、未脱酸出鋼して窒
素含有量を低下させ、スラグ除去後に取鍋で脱酸するこ
とによりAt脱酸剤の県単位を少なくしかつ脱酸の安定
性を高めることができる。
As explained above, according to the present invention, the nitrogen content is reduced by tapping undeoxidized steel, and deoxidation is performed in a ladle after removing slag, thereby reducing the amount of At deoxidizer per prefecture and increasing the deoxidation rate. Stability can be increased.

Claims (1)

【特許請求の範囲】[Claims] 転炉から未脱酸出鋼した後取鍋精錬炉でスラグを除去し
てから脱酸剤を添加する溶鋼の精錬方法。
A molten steel refining method in which undeoxidized steel is extracted from a converter, slag is removed in a ladle refining furnace, and then a deoxidizing agent is added.
JP59213330A 1984-10-12 1984-10-12 Refining method of molten steel Pending JPS6191311A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP59213330A JPS6191311A (en) 1984-10-12 1984-10-12 Refining method of molten steel
US06/782,527 US4652308A (en) 1984-10-12 1985-10-01 Process for refining molten steel
DE8585112614T DE3581475D1 (en) 1984-10-12 1985-10-04 METHOD FOR REFRESHING STEEL.
EP85112614A EP0179337B1 (en) 1984-10-12 1985-10-04 Process for refining molten steel
ZA857708A ZA857708B (en) 1984-10-12 1985-10-07 Process for refining molten steel
KR1019850007459A KR900002574B1 (en) 1984-10-12 1985-10-10 Process for refining molte steel
CA000492824A CA1244245A (en) 1984-10-12 1985-10-11 Process for refining molten steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59213330A JPS6191311A (en) 1984-10-12 1984-10-12 Refining method of molten steel

Publications (1)

Publication Number Publication Date
JPS6191311A true JPS6191311A (en) 1986-05-09

Family

ID=16637369

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59213330A Pending JPS6191311A (en) 1984-10-12 1984-10-12 Refining method of molten steel

Country Status (2)

Country Link
JP (1) JPS6191311A (en)
ZA (1) ZA857708B (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5418415A (en) * 1977-07-12 1979-02-10 Kawasaki Steel Co Method of treating molten steel for preventing nitrogen increase in steel
JPS5754216A (en) * 1980-09-16 1982-03-31 Nippon Kokan Kk <Nkk> Production of low solved aluminum steel

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5418415A (en) * 1977-07-12 1979-02-10 Kawasaki Steel Co Method of treating molten steel for preventing nitrogen increase in steel
JPS5754216A (en) * 1980-09-16 1982-03-31 Nippon Kokan Kk <Nkk> Production of low solved aluminum steel

Also Published As

Publication number Publication date
ZA857708B (en) 1986-06-25

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