JPH08302417A - Method for melting chromium steel - Google Patents

Method for melting chromium steel

Info

Publication number
JPH08302417A
JPH08302417A JP7128818A JP12881895A JPH08302417A JP H08302417 A JPH08302417 A JP H08302417A JP 7128818 A JP7128818 A JP 7128818A JP 12881895 A JP12881895 A JP 12881895A JP H08302417 A JPH08302417 A JP H08302417A
Authority
JP
Japan
Prior art keywords
molten steel
melting
mixed gas
oxygen
steel
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
JP7128818A
Other languages
Japanese (ja)
Other versions
JP3578515B2 (en
Inventor
Ryuji Nakao
隆二 中尾
Hironori Takano
博範 高野
Tetsuya Yamamoto
哲也 山本
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 JP12881895A priority Critical patent/JP3578515B2/en
Publication of JPH08302417A publication Critical patent/JPH08302417A/en
Application granted granted Critical
Publication of JP3578515B2 publication Critical patent/JP3578515B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

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

Abstract

PURPOSE: To realize the efficient melting by reducing the oxidation of [Cr] in the molten steel in the process to melt Cr steel in an electric furnace. CONSTITUTION: The mixed gas containing >=10% oxygen gas is blown into the molten steel by >=0.1Nm<3> /min per unit ton of the molten steel after >=20% of the material charged in an electric furnace is melted to become the molten steel. As the temperature of the molten steel rises, the ratio of the oxygen gas in the mixed gas is increased up to 90%. The decarburizing reaction by the oxygen in the mixed gas procedes under the condition where the oxidation of [Cr] in the molten steel is small, and the power consumption unit for melting is reduced by the decarburizing reaction heat, and the melting time is reduced.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】電気炉にて含クロム鋼を溶解する
工程において、溶鋼中の[Cr]の酸化を少なくし、溶
解時間の短縮をはかり、効率的に装入材料の溶解を図る
含クロム鋼の溶解方法に関する。
[Industrial application] In the process of melting chromium-containing steel in an electric furnace, the oxidation of [Cr] in the molten steel is reduced, the melting time is shortened and the charging material is efficiently melted. The present invention relates to a method for melting chromium steel.

【0002】[0002]

【従来の技術】ステンレス鋼のごとき11mass%以
上のCrを含むような含クロム鋼は、電気炉で素材を溶
解し、その後、上底吹き転炉、AODおよびVOD等で
精錬されて、製造されている。含クロム鋼の電気炉での
溶解は、スクラップ以外にフェロクロム、フェロニッケ
ル等の合金も溶解材料として、電気炉内に装入し材料に
通電することにより、電熱によって溶解が行われる。
2. Description of the Related Art Chromium-containing steel such as stainless steel containing 11 mass% or more of Cr is manufactured by melting a raw material in an electric furnace and then refining it in a top-bottom blowing converter, AOD and VOD. ing. For melting chromium-containing steel in an electric furnace, alloys such as ferrochromium and ferro-nickel are also used as melting materials in addition to scrap, and are charged into the electric furnace to energize the material to be melted by electric heat.

【0003】電気炉で材料溶解中に、酸素ガス(以下、
単に酸素という)や空気等の酸化性ガスを溶鋼内に吹込
む方法は、Crを含まない普通鋼の分野では広く行われ
ており、この方法により溶解時間の短縮や電力原単位の
低減等の効率的な溶解が達成されている。また、電気炉
での含クロム鋼の溶解で、酸素を溶鋼中に吹込む方法
は、AODやVODが導入される以前から行われてい
た。この方法は電気炉に装入した材料が完全に溶解し、
溶鋼温度が約1600℃以上になった時点で、溶鋼中の
[C]濃度を製品で要求される濃度まで下げるものであ
り、酸素の吹込みで[C]濃度の低下(脱炭)と同時
に、溶鋼中の[Cr]の酸化も進行するために、AOD
やVODが導入されてからは通常実施されていない。
During melting of materials in an electric furnace, oxygen gas (hereinafter,
The method of blowing an oxidizing gas such as oxygen or air into molten steel is widely used in the field of ordinary steel that does not contain Cr. This method reduces the melting time and the power consumption rate. Efficient lysis has been achieved. Further, the method of blowing oxygen into molten steel by melting chromium-containing steel in an electric furnace has been performed before the introduction of AOD or VOD. This method completely melts the material charged into the electric furnace,
When the molten steel temperature rises above about 1600 ° C, the [C] concentration in the molten steel is lowered to the concentration required by the product, and at the same time the [C] concentration decreases (decarburization) due to the blowing of oxygen. , Because oxidation of [Cr] in molten steel also progresses, AOD
It has not been implemented since the introduction of VOD and VOD.

【0004】一方、含クロム鋼の電気炉での溶解時に酸
素と窒素ガスから成る空気を吹込む方法として、特開昭
58−167714号公報が開示されている。この方法
は、溶解期、酸化期および還元期で構成される電気炉溶
解工程の中で、還元期中にアーク加熱を一時中断し、精
錬用ランスから鋼浴中に空気を吹込む方法である。この
方法では還元期の効率的な還元反応の進行は図れるが、
溶解期および酸化期での吹込みはなく、かつ還元期の吹
込みでもアーク加熱を中断して行うために、溶解時間の
短縮や溶鋼中の[Cr]酸化の防止等については十分な
効果は得られていない。
On the other hand, Japanese Patent Laid-Open No. 58-167714 discloses a method of blowing air consisting of oxygen and nitrogen gas when melting chromium-containing steel in an electric furnace. This method is a method in which arc heating is temporarily interrupted during the reduction period and air is blown into the steel bath from the refining lance in the electric furnace melting process that is composed of the melting period, the oxidation period, and the reduction period. Although this method can promote the efficient reduction reaction in the reduction period,
There is no injection during the melting period and oxidation period, and because arc heating is interrupted even during the injection during the reduction period, there is no sufficient effect in shortening the melting time and preventing [Cr] oxidation in molten steel. Not obtained.

【0005】また、含クロム鋼の電気炉での溶解時に酸
化性ガスを吹込む方法としては、特開昭52−9551
8号公報が開示されている。この方法は、電気炉内の溶
鋼に純酸素とともに水蒸気を吹入れて、[C]濃度を
0.2〜0.4mass%まで低下させる方法である。
この方法も材料が完全に溶解した後に、ガス吹込みを行
う方法であり、[C]濃度の低下によって、精錬工程の
負荷は軽減されるが、電気炉での溶解時間の短縮等の効
率的な溶解にはつながっていない。このように、従来の
技術では、酸化性ガスの吹込みによって溶解時間の短
縮、溶鋼中の[Cr]の酸化の防止に十分な効果は得ら
れておらず、十分に活用されていない状況にあった。
Further, as a method of blowing an oxidizing gas when melting chromium-containing steel in an electric furnace, Japanese Patent Laid-Open No. 52-9551 is known.
No. 8 publication is disclosed. This method is a method of injecting steam together with pure oxygen into molten steel in an electric furnace to reduce the [C] concentration to 0.2 to 0.4 mass%.
This method is also a method in which gas is blown after the material is completely melted, and the load of the refining process is reduced by lowering the concentration of [C], but the melting time in the electric furnace is shortened efficiently. It does not lead to good dissolution. As described above, in the conventional technique, the blowing time of the oxidizing gas does not bring about a sufficient effect for shortening the melting time and preventing the oxidation of [Cr] in the molten steel, and the situation is not sufficiently utilized. there were.

【0006】[0006]

【発明が解決しようとする課題】電気炉にて含クロム鋼
を溶解する工程において、溶解の途中より溶鋼中に酸素
を含む混合ガスの吹込みを行い、溶鋼中の[Cr]の酸
化を極力抑え、溶解時間の短縮をはかる効率的な溶解方
法を提供するものである。
In the process of melting chromium-containing steel in an electric furnace, a mixed gas containing oxygen is blown into the molten steel during melting so that the oxidation of [Cr] in the molten steel is minimized. The present invention provides an efficient dissolution method that suppresses and shortens the dissolution time.

【0007】[0007]

【課題を解決するための手段】本発明は上述の課題を有
利に解決したものであり、その要旨とするところは電気
炉にて含クロム鋼を溶解する工程において、該電気炉内
に装入した材料の20%以上が溶けて溶鋼となった後
に、酸素を10%以上含む混合ガスを前記溶鋼中に溶鋼
トン当り0.1Nm3 /min以上吹込むことを特徴と
する含クロム鋼の溶解方法である。また、溶鋼中に吹込
むガスが酸素と不活性ガスの混合ガスであることを特徴
とし、溶鋼温度の上昇にしたがい、混合ガス中の酸素の
比率を最大90%まで増大させることを特徴とする含ク
ロム鋼の溶解方法にある。なお、溶鋼トン当りの吹込み
流量は、電気炉での溶解終了時での溶鋼量を基準とした
吹込み量である。
The present invention advantageously solves the above-mentioned problems, and the gist of the present invention is to charge a chromium-containing steel in an electric furnace in the step of melting the chromium-containing steel. After melting 20% or more of the formed material into molten steel, a mixed gas containing 10% or more oxygen is blown into the molten steel at a rate of 0.1 Nm 3 / min or more per ton of molten steel to dissolve chromium-containing steel. Is the way. Further, the gas blown into the molten steel is a mixed gas of oxygen and an inert gas, and the ratio of oxygen in the mixed gas is increased up to 90% as the molten steel temperature rises. It is a method of melting chromium-containing steel. The blowing flow rate per ton of molten steel is the blowing amount based on the molten steel amount at the end of melting in the electric furnace.

【0008】[0008]

【作用】以下、本発明について詳細に説明する。本発明
の電気炉にて含クロム鋼を溶解する工程において、酸素
を含む混合ガスを吹込む方法は、図1に例示するような
方法によって行う。図1の(a)は底吹きノズルあるい
は底吹き羽口から酸素を含む混合ガスを吹込む方法、
(b)は炉口より上吹きランスを挿入してランスから酸
素を含む混合ガスを吹込む方法を示した。図中の1は電
気炉炉体、2は電極、3は溶鋼、4は未溶解の材料、5
はアーク、6は底吹きノズルあるいは底吹き羽口、7は
上吹きランスを示す。本発明は、図1の(a)および
(b)に例示するように、電気炉内に装入した材料が、
完全に溶解を完了していない時点より、溶鋼中に酸素を
含む混合ガスを吹込む方法である。
The present invention will be described in detail below. In the step of melting the chromium-containing steel in the electric furnace of the present invention, the method of blowing the mixed gas containing oxygen is performed by the method illustrated in FIG. FIG. 1 (a) shows a method of blowing a mixed gas containing oxygen from a bottom blowing nozzle or a bottom blowing tuyere,
(B) shows a method of inserting an upper blowing lance from the furnace opening and blowing a mixed gas containing oxygen from the lance. In the figure, 1 is an electric furnace body, 2 is an electrode, 3 is molten steel, 4 is unmelted material, 5
Is an arc, 6 is a bottom blowing nozzle or bottom blowing tuyere, and 7 is a top blowing lance. The present invention, as illustrated in FIGS. 1 (a) and 1 (b), shows that the material charged in the electric furnace is
This is a method in which a mixed gas containing oxygen is blown into the molten steel from the time when the melting is not completely completed.

【0009】図2は、SUS304ステンレス鋼を電気
炉で溶解した場合、酸素を含む混合ガスの吹込みを開始
する時点で、装入した材料の溶解して溶鋼になった比率
と、溶鋼中の[Cr]の酸化指数の関係を示す。なお、
[Cr]の酸化指数は、装入した材料が100%溶解し
た時点より混合ガスの吹込みを行った場合の、溶鋼中の
[Cr]の酸化量の平均値を100として、比例概算し
た値である。また、混合ガスの吹込み流量は溶鋼トン当
りの0.01Nm3 /minから0.2Nm3 /min
の範囲で行い、混合ガスとしては酸素を10〜30%含
む、アルゴンあるいは窒素ガスとの混合ガスを用いた。
図2より、装入した材料の溶解した比率が20%未満で
は急激に[Cr]の酸化量が増大する。これより、[C
r]の酸化を防止するために、混合ガスの吹込みを開始
するのは装入した材料が20%以上溶解した時点より行
う必要がある。
FIG. 2 shows that when SUS304 stainless steel is melted in an electric furnace, the ratio of the charged material to the melted steel at the time when the injection of the mixed gas containing oxygen is started, The relationship of the oxidation index of [Cr] is shown. In addition,
The oxidation index of [Cr] is a value roughly proportional to the average value of the oxidation amount of [Cr] in the molten steel as 100 when the mixed gas is blown from the time when the charged material is completely melted. Is. Further, blowing flow rate of the mixed gas is 0.2 Nm 3 / min from 0.01 Nm 3 / min per ton of the molten steel
And the mixed gas with argon or nitrogen gas containing 10 to 30% of oxygen was used as the mixed gas.
From FIG. 2, when the dissolved ratio of the charged materials is less than 20%, the amount of [Cr] oxidized rapidly increases. From this, [C
In order to prevent the oxidation of [r], it is necessary to start blowing the mixed gas from the time when the charged material is dissolved by 20% or more.

【0010】図3は、SUS304ステンレス鋼の電気
炉での溶解で、酸素を含む混合ガスの吹込みを行った場
合、溶鋼トン当りの混合ガスの吹込み流量と、溶鋼中の
[Cr]の酸化指数の関係を示す。なお、[Cr]の酸
化指数は溶鋼トン当りの混合ガスの吹込み流量が、0.
01Nm3 /minの場合の、溶鋼中の[Cr]の酸化
量の平均値を100として比例概算した値である。ま
た、混合ガスの吹込みは、装入した材料の20〜40%
が溶解した時点より開始し、混合ガスとしては、酸素を
10〜50%含むアルゴンあるいは窒素ガスとの混合ガ
スを用いた。図3より、溶鋼トン当りの混合ガスの吹込
み流量が、0.01Nm3 /min未満では急激に[C
r]の酸化量が増大しており、[Cr]の酸化を防止す
るために混合ガスの吹込み流量は、溶鋼トン当り0.0
1Nm3 /min以上にする必要がある。
FIG. 3 shows that when SUS304 stainless steel is melted in an electric furnace and a mixed gas containing oxygen is blown, the flow rate of the mixed gas per ton of molten steel and the [Cr] content in the molten steel. The relationship of the oxidation index is shown. The oxidation index of [Cr] is 0.
It is a value roughly proportionally calculated with the average value of the oxidation amount of [Cr] in the molten steel being 100 in the case of 01 Nm 3 / min. In addition, the mixed gas is blown at 20 to 40% of the charged material.
Was started from the time when was dissolved, and a mixed gas with argon or nitrogen gas containing 10 to 50% oxygen was used as the mixed gas. From FIG. 3, when the flow rate of the mixed gas blown per ton of molten steel is less than 0.01 Nm 3 / min, the [C
The amount of oxidation of r] is increasing, and the flow rate of the mixed gas is 0.0 per ton of molten steel in order to prevent the oxidation of [Cr].
It should be 1 Nm 3 / min or more.

【0011】図4は、SUS304ステンレス鋼の電気
炉での溶解で、酸素を含む混合ガスの吹込みを行った場
合、混合ガス中の酸素の比率と溶解時間の短縮率の関係
を示す。なお、溶解時間の短縮率はガス吹込みのない場
合の溶解時間に対する短縮率である。また、混合ガスの
吹込み流量は、溶鋼トン当り0.01〜0.05Nm3
/minの範囲であり、混合ガスの吹込みは装入した材
料の20〜40%が溶解した時点より開始した。図4よ
り、吹込み混合ガスの酸素ガスの比率が10%未満では
溶解時間の短縮率は非常に小さく、溶解時間の短縮をは
かり、効率的に溶解を行うには混合ガス中の酸素の比率
は10%以上にする必要がある。
FIG. 4 shows the relationship between the proportion of oxygen in the mixed gas and the shortening rate of the melting time when the mixed gas containing oxygen is blown in melting SUS304 stainless steel in an electric furnace. The rate of shortening the melting time is the rate of shortening the melting time in the absence of gas injection. The flow rate of the mixed gas blown is 0.01 to 0.05 Nm 3 per ton of molten steel.
/ Min, and the blowing of the mixed gas was started from the time when 20 to 40% of the charged material was melted. From FIG. 4, when the ratio of oxygen gas in the blown mixed gas is less than 10%, the shortening rate of the dissolution time is very small. Therefore, in order to shorten the dissolution time and efficiently perform the dissolution, the ratio of oxygen in the mixed gas is Must be 10% or more.

【0012】図5は、SUS304ステンレス鋼の電気
炉での溶解で、酸素を含む混合ガスを溶鋼トン当り0.
01〜0.20Nm3 /minの流量で吹込みを行った
場合、混合ガス中の酸素の比率と溶鋼中の[Cr]の酸
化指数の関係を示す。なお、図には混合ガスの吹込みを
開始した時点が、装入した材料の20〜40%が溶解し
た時点の場合と、80〜100%が溶解した時点の場合
を合わせて示した。また、[Cr]の酸化指数は装入し
た材料の20〜40%が溶解した時点で、混合ガスの吹
込みを行った場合の混合ガス中の酸素の比率が10%で
の溶鋼中の[Cr]の酸化量を100として比例換算し
た値である。
FIG. 5 shows melting of SUS304 stainless steel in an electric furnace, and a mixed gas containing oxygen is supplied at a rate of 0.
When blowing is performed at a flow rate of 01 to 0.20 Nm 3 / min, the relationship between the ratio of oxygen in the mixed gas and the oxidation index of [Cr] in the molten steel is shown. In addition, in the figure, the time when the injection of the mixed gas is started is shown at the time when 20 to 40% of the charged material is dissolved and the time when 80 to 100% is dissolved. In addition, the oxidation index of [Cr] is 20% to 40% of the charged material is melted, and when the mixed gas is blown, the ratio of oxygen in the mixed gas is 10%. It is a value obtained by proportionally converting the oxidation amount of Cr] as 100.

【0013】図5より、混合ガスの吹込みを開始した時
点での装入した材料の溶解した比率が高い側、つまり溶
鋼温度の高い側の方が吹込みガスの酸素の比率を高くし
ても[Cr]の酸化が抑えられる。また、装入した材料
の溶解比率が高い側でも吹込みガスの酸素の比率が90
%を越えると、[Cr]の酸化が急激に増大する。従っ
て、溶鋼温度の上昇にしたがい、混合ガス中の酸素の比
率を最大90%まで増大させることで、[Cr]の酸化
を抑え効率的な脱炭が可能であることがわかる。
As shown in FIG. 5, the oxygen content of the blowing gas is increased on the side where the ratio of the melted materials at the time of starting the injection of the mixed gas is high, that is, the side where the molten steel temperature is high. Also suppresses the oxidation of [Cr]. In addition, even if the dissolved ratio of the charged material is high, the oxygen ratio of the blown gas is 90%.
When it exceeds%, the oxidation of [Cr] rapidly increases. Therefore, it is understood that by increasing the ratio of oxygen in the mixed gas up to 90% as the molten steel temperature rises, the oxidation of [Cr] can be suppressed and efficient decarburization can be performed.

【0014】以上より、電気炉にて含クロム鋼を溶解す
る工程において、電気炉内に装入した材料の20%以上
が溶けて溶鋼となった後に、酸素を10%以上含む混合
ガスを溶鋼トン当り0.01Nm3 /min以上吹込む
ことにより、溶鋼中の[Cr]の酸化が少なく、溶解時
間が短縮されて効率的な溶解が可能になる。また、前記
溶鋼温度が上昇するにしたがい、混合ガス中の酸素ガス
の比率を最大90%まで増大させる方法が有効である。
操業においては、装入した材料の溶けて溶鋼になった比
率は総電力投入量より把握することが可能であり、総電
力量の推移にしたがい、混合ガスの吹込み流量および酸
素の比率を調整すればよい。
From the above, in the step of melting chromium-containing steel in an electric furnace, 20% or more of the material charged in the electric furnace is melted into molten steel, and then a mixed gas containing 10% or more oxygen is melted. By blowing 0.01 Nm 3 / min or more per ton, the oxidation of [Cr] in the molten steel is small, the melting time is shortened, and efficient melting becomes possible. Further, it is effective to increase the ratio of oxygen gas in the mixed gas up to 90% as the molten steel temperature rises.
In operation, it is possible to understand the ratio of the charged materials that have melted to become molten steel from the total power input.Adjust the flow rate of the mixed gas and the oxygen ratio according to the change in the total power input. do it.

【0015】この混合ガスの吹込みによって、溶鋼中の
[C]および[Si]の酸化が進行するために、この酸
化反応熱によって溶解が促進され、溶解時間の短縮およ
び溶解電力原単位の低減につながる。なお、溶鋼中の
[C]濃度は0.5mass%以下になると[Cr]の
酸化が進行しやすくなるために、この値以上に[C]濃
度を保持できるように、全酸素の吹込み流量を調整する
ことが好ましい。また、吹込み混合ガス流量の上限は、
炉内の攪拌状態に依存し、炉形状によって決まる値であ
るが、一般的には溶鋼トン当り0.5Nm3 /min以
下が好ましい。
By blowing the mixed gas, the oxidation of [C] and [Si] in the molten steel proceeds, so that the heat of oxidation reaction promotes the melting, which shortens the melting time and reduces the unit consumption of the melting power. Leads to. If the [C] concentration in the molten steel becomes 0.5 mass% or less, the oxidation of [Cr] is likely to proceed. Therefore, in order to maintain the [C] concentration above this value, the total oxygen flow rate Is preferably adjusted. Also, the upper limit of the flow rate of the mixed gas blown is
The value depends on the state of stirring in the furnace and is determined by the shape of the furnace, but is generally preferably 0.5 Nm 3 / min or less per ton of molten steel.

【0016】含クロム鋼を電気炉で溶解する工程では、
溶解材料としてスクラップ以外にフェロクロム、フェロ
ニッケル等の合金が用いられることが一般的である。こ
れらの材料にはCが含まれており、酸素を含むガスの吹
込みを行わなかった場合には、溶解終了時点で[C]濃
度は1〜3mass%になる。
In the process of melting chromium-containing steel in an electric furnace,
In addition to scrap, alloys such as ferrochrome and ferronickel are generally used as the melting material. These materials contain C, and when the gas containing oxygen is not blown in, the [C] concentration becomes 1 to 3 mass% at the end of melting.

【0017】含クロム溶鋼に酸素を含むガスを吹込んだ
場合には、下記(1)式に示す脱炭反応が進行すると同
時に、下記(3)式に示す溶鋼中の[Cr]の酸化反応
が進行する可能性がある。なお、(1)式の反応の平衡
定数Kは(2)式で表される。
When a gas containing oxygen is blown into the chromium-containing molten steel, the decarburization reaction shown in the following formula (1) proceeds and at the same time, the oxidation reaction of [Cr] in the molten steel shown in the following formula (3). May progress. The equilibrium constant K of the reaction of the equation (1) is expressed by the equation (2).

【0018】[0018]

【数1】 [Equation 1]

【0019】ここで、PCOは雰囲気中のCOガス分圧
(atm)、aC ,aO は溶鋼中の[C]および[O]
の活量、Tは溶鋼温度(K)を夫々示す。(3)式の
[Cr]の酸化反応の進行を抑え、(1)式の脱炭反応
を効率的に進行させるには(2)式より、COガス分圧
COの低下および溶鋼温度Tの上昇が有効である。
Here, P CO is the partial pressure (atm) of CO gas in the atmosphere, and a C and a O are [C] and [O] in the molten steel.
, T indicates the molten steel temperature (K), respectively. (3) suppressing the progress of oxidation reaction of [Cr] of formula (1) of the advancing the decarburization reaction efficiently than (2), lowered and the molten steel temperature of the CO gas partial pressure P CO T Is effective.

【0020】従来、AODやVOD等の精錬炉では、1
650℃以上の高温下でPCOの低下が可能であり、効率
的な脱炭が可能であった。一方、電気炉のような溶解炉
では、室温あるいは数百℃レベルより溶解を開始するた
めに、酸素単独の吹込みでは急激な[Cr]の酸化反応
が進行し、効率的な脱炭および溶解は達成することが出
来なかった。さらに、電気炉は一般的には底吹きのガス
攪拌がなく、溶鋼の攪拌が弱いために、溶解中に雰囲気
中に存在する酸素によって、[Cr]の酸化が進行する
ために、溶解後、酸化した[Cr]を回収するための還
元処理が行われてきた。
Conventionally, in refining furnaces such as AOD and VOD, 1
It was possible to reduce PCO at a high temperature of 650 ° C. or higher, and efficient decarburization was possible. On the other hand, in a melting furnace such as an electric furnace, since melting starts at room temperature or at a level of several hundreds of degrees Celsius, a rapid oxidation reaction of [Cr] progresses by blowing oxygen alone, resulting in efficient decarburization and melting. Could not be achieved. Further, since the electric furnace generally has no bottom-blown gas agitation and the agitation of molten steel is weak, the oxidation of [Cr] progresses due to the oxygen existing in the atmosphere during the melting. Reduction treatments have been performed to recover the oxidized [Cr].

【0021】このような状況下で、本発明者らは、酸素
とアルゴン、窒素等の不活性ガスの混合ガスを溶鋼中に
吹込めば、アルゴン、窒素がPCOの低下に作用すること
を見い出した。また、電気炉内に装入した材料の20%
以上が溶けて溶鋼となった状態であれば、溶鋼温度が前
記(3)式の[Cr]の酸化反応よりも、前記(1)式
の脱炭反応が促進される条件が達成され、酸素を10%
以上含む混合ガスの吹込みが可能になることを見い出し
た。さらに、雰囲気からの[Cr]の酸化を進行させな
い条件として、溶鋼トン当り0.01Nm3 /min以
上の混合ガスの吹込めばよいことも見い出した。
[0021] Under such circumstances, the present inventors have found that, oxygen and argon, if put blown into the molten steel a mixed gas of an inert gas such as nitrogen, that argon, nitrogen acts to decrease in P CO I found it. In addition, 20% of the material charged in the electric furnace
In the state where the above is melted into molten steel, the conditions in which the molten steel temperature promotes the decarburization reaction of the above formula (1) rather than the oxidation reaction of [Cr] of the above formula (3) is achieved, and oxygen 10%
It has been found that it is possible to inject the mixed gas containing the above. Furthermore, it was found that a mixed gas of 0.01 Nm 3 / min or more per ton of molten steel should be blown in as a condition for preventing the oxidation of [Cr] from the atmosphere.

【0022】これらの条件によって、[Cr]の酸化を
極力少なくして、脱炭反応が進行することになるが、脱
炭反応量を増加させるためには溶解比率の増大、つまり
溶鋼温度の上昇にしたがい、混合ガス中の酸素の比率を
最大90%までを増大させることが特に有効であること
を見い出した。このような条件での混合ガスの吹込みに
より、前記(1)式の反応が進行し、生成したCOガス
の一部または全部が雰囲気中に存在する酸素と反応し
て、下記(4)式の二次燃焼反応が進行する。
Under these conditions, the oxidation of [Cr] is minimized and the decarburization reaction proceeds, but in order to increase the decarburization reaction amount, the melting ratio is increased, that is, the molten steel temperature is increased. Accordingly, it has been found that increasing the proportion of oxygen in the mixed gas up to 90% is particularly effective. By injecting the mixed gas under such conditions, the reaction of the above formula (1) proceeds, and a part or all of the generated CO gas reacts with oxygen present in the atmosphere to generate the following formula (4). Secondary combustion reaction proceeds.

【0023】[0023]

【数2】 [Equation 2]

【0024】(1)式および(4)式の反応とも発熱反
応であり、溶鋼温度が上昇し、溶解時間の短縮および溶
解電力原単位の低減につながる。なお、(1)式の反応
進行により、溶鋼中の[C]濃度が低下する。[C]濃
度が約0.5mass%以下になると(3)式の[C
r]の酸化反応が進行しやすくなるために、電気炉での
溶解終了時の[C]濃度は、この程度以上にすることが
好ましい。
Both the reactions of the equations (1) and (4) are exothermic reactions, and the temperature of the molten steel rises, which leads to a reduction in the melting time and a reduction in the basic unit of melting power. Note that the [C] concentration in the molten steel decreases as the reaction of formula (1) progresses. When the concentration of [C] is about 0.5 mass% or less, the [C
The [C] concentration at the end of melting in the electric furnace is preferably at or above this level because the oxidation reaction of [r] easily proceeds.

【0025】[0025]

【実施例】SUS304ステンレス鋼(8mass%N
i−18mass%Cr)の電気炉での溶解時に酸素と
窒素ガスとの混合ガスを吹込む処理を図1(a)に示す
実施態様で実施した。溶解材料には、スクラップ、フェ
ロクロム、フェロニッケルを用い、酸素を含む酸化性ガ
スの吹込みのない場合には、溶解後の[C]濃度は1.
8〜2.0mass%の範囲になる条件で、溶鋼60t
を製造した。溶解後、溶解中に酸化した[Cr]を還元
するためにFe−Siを添加して還元処理を行い、取鍋
に出鋼し、その後、AODでの脱炭および脱硫処理等を
行った後に、連続鋳造機による鋳造を行い、鋳片を製造
した。
[Example] SUS304 stainless steel (8 mass% N
A process of blowing a mixed gas of oxygen and nitrogen gas at the time of melting (i-18 mass% Cr) in an electric furnace was carried out in the embodiment shown in FIG. Scrap, ferrochromium, or ferronickel is used as the melting material, and when the oxidizing gas containing oxygen is not blown, the [C] concentration after melting is 1.
Molten steel 60t under the condition of 8 to 2.0 mass%
Was manufactured. After melting, Fe-Si was added to reduce [Cr] that was oxidized during melting, reduction treatment was performed, steel was tapped, and then decarburization and desulfurization treatment with AOD was performed. Casting was performed by casting with a continuous casting machine.

【0026】表1に電気炉での溶解時の酸素を含む混合
ガスの吹込み条件の実施例を示す。本発明の実施例は、
先に示した条件を満足するように実施し、装入した材料
の溶解した比率が増加するにしたがい、混合ガス中の酸
素の比率を増大させた。比較例のNo.6はガスの吹込
みのない例、No.7は酸素単独の吹込みを行った例、
No.8は吹込み開始時期が本発明の条件外の例、N
o.9は吹込み混合ガスの量が本発明の条件外の例であ
る。
Table 1 shows examples of blowing conditions of a mixed gas containing oxygen during melting in an electric furnace. Examples of the present invention include
It was carried out so as to satisfy the conditions shown above, and the proportion of oxygen in the mixed gas was increased as the dissolved proportion of the charged materials increased. No. of the comparative example. No. 6 is an example in which no gas is blown, No. 6 7 is an example of blowing oxygen alone,
No. 8 is an example in which the blowing start time is outside the conditions of the present invention, N
o. 9 is an example in which the amount of the blown mixed gas is outside the conditions of the present invention.

【0027】[0027]

【表1】 [Table 1]

【0028】[0028]

【表2】 [Table 2]

【0029】実施結果を表2に示す。表中の値は比較例
のNo.6の結果を100として、比較換算した値であ
る。本発明例では、ガス吹込みのない場合に比べ、溶鋼
中の[Cr]の酸化はほぼ同等レベル以下であるため
に、還元用Siの添加量も同等レベル以下であり、電力
原単位の低減、溶解時間の短縮、さらには精錬時間の短
縮にもなり大幅な製造コストの低減が達成された。一
方、比較例では、ガス吹込みのない場合に比べ、電力原
単位の若干の低減および溶解時間の短縮はあるが、溶鋼
中の[Cr]の酸化が大きいために、十分な効果は得ら
れなかった。
The execution results are shown in Table 2. The values in the table are the numbers of the comparative example. The result of 6 is set to 100, and the value is comparatively converted. In the example of the present invention, the oxidation of [Cr] in the molten steel is at almost the same level or less as compared with the case where no gas is blown, so the addition amount of reducing Si is also at the same level or less, and the power consumption rate is reduced. In addition, the melting time was shortened and the refining time was also shortened, resulting in a significant reduction in manufacturing cost. On the other hand, in the comparative example, although there is a slight reduction in the electric power consumption rate and a reduction in the melting time as compared with the case where no gas is blown in, a sufficient effect can be obtained because the oxidation of [Cr] in the molten steel is large. There wasn't.

【0030】[0030]

【発明の効果】本発明法によると、電気炉での含クロム
鋼の溶解において、溶鋼中の[Cr]の酸化を抑制した
条件で、溶鋼の脱炭が進行するために溶解時間の大幅な
短縮、電力原単位の低減が達成され、併せて、その後の
工程である精錬時間の短縮も達成されて、製造コストの
低減および生産性の大幅な向上が達成される。
According to the method of the present invention, in the melting of chromium-containing steel in an electric furnace, decarburization of the molten steel proceeds under the condition that the oxidation of [Cr] in the molten steel is suppressed. Shortening and reduction of power consumption are achieved, and at the same time, shortening of the refining time which is the subsequent process is also achieved, resulting in reduction of manufacturing cost and significant improvement of productivity.

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

【図1】本発明の実施態様例の酸素を含む混合ガスの吹
込み方法を示す図
FIG. 1 is a diagram showing a method for injecting a mixed gas containing oxygen according to an embodiment of the present invention.

【図2】本発明法における酸素を含む混合ガスの吹込み
開始する条件の限定理由を示す図
FIG. 2 is a diagram showing the reason for limiting the conditions for starting the injection of a mixed gas containing oxygen in the method of the present invention.

【図3】本発明法における酸素を含む混合ガスの吹込み
流量の限定理由を示す図
FIG. 3 is a diagram showing the reason for limiting the flow rate of the mixed gas containing oxygen in the method of the present invention.

【図4】本発明法における吹込み混合ガス中の酸素の比
率の限定理由を示す図
FIG. 4 is a diagram showing the reason for limiting the ratio of oxygen in the blown mixed gas in the method of the present invention.

【図5】本発明法における吹込む混合ガス中の酸素の比
率の変化を説明する図
FIG. 5 is a diagram for explaining changes in the ratio of oxygen in the mixed gas to be blown in the method of the present invention.

【符号の説明】[Explanation of symbols]

1 電気炉炉体 2 電極 3 溶鋼 4 未溶解材料 5 アーク 6 底吹きノズル 7 上吹きランス 1 Electric Furnace Body 2 Electrode 3 Molten Steel 4 Unmelted Material 5 Arc 6 Bottom Blowing Nozzle 7 Top Blowing Lance

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 電気炉にて含クロム鋼を溶解する工程に
おいて、該電気炉内に装入した材料の20%以上が溶け
て溶鋼となった後に、酸素を10%以上含む混合ガスを
前記溶鋼中に溶鋼トン当り0.1Nm3 /min以上吹
込むことを特徴とする含クロム鋼の溶解方法。
1. In a step of melting chromium-containing steel in an electric furnace, 20% or more of a material charged in the electric furnace is melted to form molten steel, and then a mixed gas containing 10% or more of oxygen is added. A method for melting chromium-containing steel, which comprises injecting 0.1 Nm 3 / min or more per ton of molten steel into the molten steel.
【請求項2】 溶鋼中に吹込むガスが酸素と不活性ガス
の混合ガスであることを特徴とする請求項1記載の含ク
ロム鋼の溶解方法。
2. The method for melting chromium-containing steel according to claim 1, wherein the gas blown into the molten steel is a mixed gas of oxygen and an inert gas.
【請求項3】 溶鋼温度の上昇にしたがい、混合ガス中
の酸素の比率を最大90%まで増大させることを特徴と
する請求項1記載の含クロム鋼の溶解方法。
3. The method for melting chromium-containing steel according to claim 1, wherein the ratio of oxygen in the mixed gas is increased to a maximum of 90% as the molten steel temperature rises.
JP12881895A 1995-05-01 1995-05-01 Melting method of chromium-containing steel Expired - Lifetime JP3578515B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12881895A JP3578515B2 (en) 1995-05-01 1995-05-01 Melting method of chromium-containing steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12881895A JP3578515B2 (en) 1995-05-01 1995-05-01 Melting method of chromium-containing steel

Publications (2)

Publication Number Publication Date
JPH08302417A true JPH08302417A (en) 1996-11-19
JP3578515B2 JP3578515B2 (en) 2004-10-20

Family

ID=14994182

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
JP (1) JP3578515B2 (en)

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