JPS63105915A - Method for producing steel containing low phosphorous and chromium - Google Patents

Method for producing steel containing low phosphorous and chromium

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Publication number
JPS63105915A
JPS63105915A JP25002186A JP25002186A JPS63105915A JP S63105915 A JPS63105915 A JP S63105915A JP 25002186 A JP25002186 A JP 25002186A JP 25002186 A JP25002186 A JP 25002186A JP S63105915 A JPS63105915 A JP S63105915A
Authority
JP
Japan
Prior art keywords
molten steel
chromium
phosphorus
chromium oxide
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
JP25002186A
Other languages
Japanese (ja)
Inventor
Yoshimasa Mizukami
水上 義正
Hiroshi Shima
嶋 宏
Michiyasu Nozu
野津 道泰
Shinobu Oura
大浦 忍
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 JP25002186A priority Critical patent/JPS63105915A/en
Publication of JPS63105915A publication Critical patent/JPS63105915A/en
Pending legal-status Critical Current

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  • Treatment Of Steel In Its Molten State (AREA)

Abstract

PURPOSE:To omit dephosphorizing treating process, to enable Cr addition within the ordinary degassing treating time and to easily, surely and efficiently produce the titled molten steel by injecting Cr oxide into the molten steel containing the specific composition of low P and Cr by inert gas. CONSTITUTION:In the molten steel 2 containing <=0.30% C, <=100ppm P, >=0.050% Al, an uptake tube 4 and a downtake tube 3 of a vacuum degassing apparatus is immersed and the pressure in a vacuum vessel 5 is reduced and by blowing circulating gas, that is, the inert gas, such as Ar gas, etc., from a tuyere 6, the molten gas 2 is introduced into the vessel 5 to execute the degassing. Then, the chromium oxide having <=5mm diameter is injected from a tuyere 7 arranged at the vessel 5 bottom part by the inert gas, and by the soluble Al in the molten steel 2, the chromium oxide is reduced to produce the above molten steel.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は低燐クロム含有銅の溶製方法に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a method for melting copper containing low phosphorous and chromium.

(従来の技術) 近年、耐蝕性及び焼き入れ性向上の観点から、クロム含
有溶鋼の溶製′jIkは益々増加する傾向にある。又、
低温靭性向上の観点からは溶鋼の低燐化処理が必要にな
シつつある。クロム含有溶鋼の溶製方法としては、溶鋼
中に金属クロム或いはフェロクロムを添加する方法以外
に、転炉型精錬容器内の鉄浴中に、炉底から微粉状のク
ロム鉱石を吹き込み鋼浴中の炭材で還元する方法(特開
昭61−153223号公報)があるが、この方法は炭
材から燐が入る為、低燐クロム含有銅を溶製するには好
ましくない。又、溶鋼の脱燐方法としては酸化脱燐方法
と還元脱燐方法とがあシ、酸化脱燐による一般的な低燐
化処理方法としては、転炉からの溶鋼を出鋼する際、生
石灰、酸化鉄、蛍石からなる脱燐剤を溶鋼に添加して脱
燐する方法(特開昭59−490310号公報)、低燐
溶鋼中に合金鉄及び生石灰、ば化鉄、蛍石からなる脱燐
剤を添加して、温度制御しながら脱燐する方法(特開昭
60−92416号公報)等が開示されている。これら
の処理方法は溶鋼の低燐化に非常に効果がある方法であ
シ、この低燐化処理した溶鋼に燐含有蓋の少ない金属ク
ロム等を添加すれば、低燐のクロム含有溶鋼の溶製は可
能となる。しかし・燐含有量の少ない金属クロム等は非
常に高価であるため、低燐クロム含有銅の溶!!!費を
高める等の問題がある。従って、釜属クロムより比較的
安価なフェロクロム等のクロム含有合金鉄を用いること
になるが、クロム含有合金鉄中の燐が高いため・クロム
含有溶鋼の燐含有量も高くなシ、クロム含有溶鋼の脱燐
が必要となる。そこで、燐含有量の鍋いクロム含有溶鋼
を上記脱燐方法で処理すると溶鋼中クロムが脱燐剤てよ
)酸化し、クロム歩留が低下する等の問題があった。従
って、高クロム溶鋼を脱燐するための他の方法としては
金属カルシウム等による還元脱燐方法が検討されている
が、還元脱燐方法は脱燐処理後スラグ中に燐化カルシウ
ムが存在し、この燐化カルシウムが大気中の水分と反応
し、有毒なフォスフインを発生することから、脱燐後の
スラグ処理に問題を残している。
(Prior Art) In recent years, from the viewpoint of improving corrosion resistance and hardenability, there has been a tendency for the production of chromium-containing molten steel to increase more and more. or,
From the perspective of improving low-temperature toughness, phosphorous reduction treatment of molten steel is becoming necessary. In addition to adding metallic chromium or ferrochrome to molten steel, methods for producing chromium-containing molten steel include injecting finely powdered chromium ore into the iron bath in a converter-type refining vessel from the bottom of the furnace. There is a method of reduction with carbonaceous material (Japanese Unexamined Patent Publication No. 153223/1983), but this method is not preferable for melting copper containing low phosphorus and chromium because phosphorus enters from the carbonaceous material. In addition, there are two methods for dephosphorizing molten steel: oxidative dephosphorization and reductive dephosphorization.The general oxidative dephosphorization treatment method uses quicklime when tapping molten steel from a converter. , a method of dephosphorizing by adding a dephosphorizing agent consisting of iron oxide and fluorite to molten steel (Japanese Unexamined Patent Publication No. 59-490310), a method of dephosphorizing by adding a dephosphorizing agent consisting of iron oxide and fluorite to molten steel (JP-A-59-490310); A method of adding a dephosphorizing agent and dephosphorizing while controlling the temperature (Japanese Patent Application Laid-Open No. 60-92416) has been disclosed. These treatment methods are very effective in reducing phosphorus in molten steel.If metal chromium, etc., which has a low phosphorus content, is added to molten steel that has undergone low phosphorus treatment, it can be used to reduce phosphorus in molten steel. It is now possible to manufacture However, metals such as chromium with low phosphorus content are very expensive, so it is difficult to melt copper with low phosphorus content! ! ! There are problems such as increased costs. Therefore, a chromium-containing ferroalloy such as ferrochrome, which is relatively cheaper than pot metal chromium, is used. Dephosphorization is required. Therefore, when chromium-containing molten steel with a phosphorous content is treated by the above-mentioned dephosphorization method, the chromium in the molten steel is oxidized (by the dephosphorizing agent), causing problems such as a decrease in chromium yield. Therefore, as another method for dephosphorizing high-chromium molten steel, a reductive dephosphorization method using metallic calcium, etc. is being considered, but in the reductive dephosphorization method, calcium phosphide is present in the slag after the dephosphorization treatment. This calcium phosphide reacts with moisture in the atmosphere and generates toxic phosphine, which poses a problem in slag treatment after dephosphorization.

(発明が解決しようとする問題点り 本発明は上記問題点を解決し、安価に且つ効率的に低燐
クロム含有溶鋼を溶製するために開発されたものである
(Problems to be Solved by the Invention) The present invention was developed to solve the above-mentioned problems and to produce low-phosphorus-chromium containing molten steel at low cost and efficiently.

(問題点を解決するための手段) その特徴とするところは、炭素が0.30%以下、燐1
00 ppm以下、可溶性アルミニウムを050%以上
含有する溶鋼中に直径!l)l!II+以下のクロム酸
化物を不活性ガスを用いて吹き込み、可溶性アルミニウ
ムでクロム酸化物を還元することを特徴とする低燐クロ
ム含有銅の溶製方法である。
(Means to solve the problem) Its characteristics include less than 0.30% carbon and 1% phosphorus.
Diameter in molten steel containing 0.00 ppm or less and 0.50% or more of soluble aluminum! l)l! This is a method for melting copper containing low phosphorus and chromium, which is characterized by blowing in chromium oxide of II+ or less using an inert gas and reducing the chromium oxide with soluble aluminum.

一般に、クロム含有銅はその要求材質特性から低燐化と
同時に、低硫化、低酸素化、低水素化も要求される。従
って、通常はフェロクロム等のクロム合釡を低燐溶鋼に
添加した後、更に、溶鋼脱硫を行うが、脱硫効率をあげ
るため、アルミニウム、シリコン等を用いた強脱酸によ
り溶鋼中の酸素を下げた状態で脱硫を行うことが多い。
In general, chromium-containing copper is required to have low phosphorous properties, as well as low sulfidation, low oxygen, and low hydrogen levels due to its required material properties. Therefore, desulfurization of the molten steel is usually performed after adding chromium alloy such as ferrochrome to low-phosphorus molten steel. However, in order to increase the desulfurization efficiency, strong deoxidation using aluminum, silicon, etc. is used to lower the oxygen in the molten steel. Desulfurization is often carried out in the same condition.

このように、鋼材に必要とする合金成分に調贅した後、
真空脱ガス処理によプ・溶鋼中の水素ガスを除去し・目
的の溶鋼とする。
In this way, after adjusting the alloy components required for steel materials,
Vacuum degassing treatment removes hydrogen gas from the molten steel and produces the desired molten steel.

本発明は、上記通常の製造方法の中で、例えば、脱燐工
程を省略しても、低燐クロム溶鋼の溶製を可能にしたも
のである。上記通常の溶製方法で脱燐工程が必要な理由
はフェロクロムから持ち込まれる燐を除去するために行
っている。
The present invention makes it possible to produce low-phosphorus-chromium molten steel even if, for example, the dephosphorization step is omitted in the above-mentioned normal production method. The reason why the dephosphorization step is necessary in the above-mentioned normal melting method is to remove phosphorus brought in from ferrochrome.

本発明は、クロム源として燐の低い酸化クロムを用いる
ことによシ、例えば、脱燐工程を省略し、安価に低燐ク
ロム鋼ヲ溶製しようとするものである。一般に溶鋼中に
酸化クロムを添加しただけでは、鈑化クロムは還元され
ず、従って、溶鋼中に酸化物として存在することになシ
、必要とされる金属クロムは生成しないばかシか、むし
ろ、溶鋼の清浄性を悪くし、材質特性を低下させること
になる。
The present invention attempts to produce low-phosphorus chromium steel at low cost by using chromium oxide with low phosphorus content as a chromium source, for example, by omitting the dephosphorization process. Generally, simply adding chromium oxide to molten steel does not reduce the chromium platen, so it does not exist as an oxide in the molten steel, and the necessary metallic chromium is not produced, or rather, This will impair the cleanliness of the molten steel and reduce the material properties.

しかして、本発明のように、炭素が0.30%以下、燐
100 ppm以下、可溶性アルミニウムをO50%以
上含有する溶鋼中に直径5燗以下のクロム酸化物を不活
性ガスを用いて吹き込むと、クロム酸化物は溶鋼中の可
溶性アルミニウムとfIJ式のような反応を生じ、雀属
クロムとアルミナが生成する。
However, as in the present invention, if chromium oxide with a diameter of 5 or less is blown into molten steel containing 0.30% or less carbon, 100 ppm or less phosphorus, and 50% or more soluble aluminum using an inert gas, Chromium oxide reacts with soluble aluminum in molten steel in a manner similar to the fIJ formula, producing chromium and alumina.

Cr203 +2 Aj =2 (! r + A)z
ol・・・・(■)この場合、溶鋼中の炭素含有量は高
い程、反応効率は良くなるが、通常の低燐クロム含有銅
は0.30%以下である。従って、炭素濃度を高くし、
反応効率を扁めると、再度溶鋼中の炭素金工ける処理工
程が必要にな9、生産性、コスト等の点から好筐しくな
い。このため、工業的には、溶鋼中の炭素含有量は0.
30%以下にし、反応効率をあげるために、可溶性アル
ミニウムの娘度全通性範囲に特定するものである。
Cr203 +2 Aj =2 (! r + A)z
ol... (■) In this case, the higher the carbon content in the molten steel, the better the reaction efficiency, but the usual low phosphorus chromium content copper is 0.30% or less. Therefore, increasing the carbon concentration,
If the reaction efficiency is reduced, a treatment step for re-treating the molten steel with carbon metal becomes necessary9, which is unfavorable from the viewpoint of productivity, cost, etc. Therefore, industrially, the carbon content in molten steel is 0.
In order to reduce the amount to 30% or less and increase the reaction efficiency, the daughter degree of soluble aluminum is specified to be in the total passability range.

本発明では溶鋼中に可溶性アルミニウムi0.050比
以上含有させることが必要である。本発明者らはクロム
酸化物の還元におよぼす溶鋼中の可溶性アルミニウムの
含有量の影響を種々研究した。その結果を第1図に示す
。この図よシ、溶鋼(C:0.10%、Si:0.25
%、Mn:0.95%、P:0.0015%、S:O,
0O15%、Fe :残りう中の可溶性アルミニウム’
ji0.050%以上含有させることにより、工業的に
実施可能な還元率70%が確保できることが分かる。こ
のことより可溶性アルミニウムの含有量は0.050%
以上にする必要がある。更に、可溶性アルミニウムを増
加させるとクロムぼ化物の還元率は上昇しているが、可
溶性アルミニウムを高くすると、アルミニウム使用量が
多くな)、溶製費用が高くなる等の問題がある。従って
、工業的には可溶性アルミニウムは0.05%以上、0
.20%以下の範囲にするのが望ましい。
In the present invention, it is necessary to contain soluble aluminum i in a ratio of 0.050 or more in the molten steel. The present inventors conducted various studies on the influence of the content of soluble aluminum in molten steel on the reduction of chromium oxide. The results are shown in FIG. This figure shows molten steel (C: 0.10%, Si: 0.25
%, Mn: 0.95%, P: 0.0015%, S: O,
0O15%, Fe: Soluble aluminum in the remaining cavity'
It can be seen that by containing ji0.050% or more, an industrially viable reduction rate of 70% can be ensured. From this, the content of soluble aluminum is 0.050%
It is necessary to do more than that. Furthermore, although increasing the soluble aluminum content increases the reduction rate of chromium oxides, increasing the soluble aluminum content results in problems such as a large amount of aluminum used) and an increase in melting costs. Therefore, industrially, soluble aluminum is 0.05% or more, 0.
.. It is desirable to keep it within a range of 20% or less.

又本発明者らは絃化クロムの形状についても種々の研究
をした。その結果を第2図に示す。炭素含有量と可溶性
アルミニウムの含有量を一定にした場合、−足時間内で
のクロムば化物の還元率はクロム酸化物の直径が5朔以
下になると著しく増大する。従って、生産性の観点から
、クロム酸化物の直径は5闇以下にする必要がある。更
に、クロム酸化物の直径を小さくするとその後も還元率
は徐々に上昇しているが、クロム酸化物の破砕費は級数
的に増大するため、還元率が向上することによる効果よ
り、破砕費の方が高くなる。本発明者らの検討によれば
、工業的にはクロム酸化物の直径は0.1m1以上、5
W+以下で使用するのが望ましい。尚、吹き込みガスと
してはアルゴンガス或いは窒素ガスを用いるが、窒素ガ
スは溶鋼中窒素を増大させる等の問題があるため、一般
にはアルゴンガスを用いるのが良い。
The present inventors also conducted various studies regarding the shape of the chromium string. The results are shown in FIG. When the carbon content and the soluble aluminum content are held constant, the reduction rate of chromium oxide in a time period increases significantly when the diameter of the chromium oxide is less than 5 mm. Therefore, from the viewpoint of productivity, the diameter of the chromium oxide needs to be 5 mm or less. Furthermore, when the diameter of the chromium oxide is made smaller, the reduction rate gradually increases, but the crushing cost of the chromium oxide increases exponentially, so the effect of improving the reduction rate is outweighed by the crushing cost. It will be more expensive. According to the studies conducted by the present inventors, the diameter of chromium oxide is industrially 0.1 m1 or more, 5 m1 or more.
It is desirable to use it below W+. Incidentally, argon gas or nitrogen gas is used as the blowing gas, but since nitrogen gas has problems such as increasing nitrogen in the molten steel, it is generally better to use argon gas.

次に実施方法について説明する。転炉で溶製した炭素0
.30%以下、燐30 ppm以下の溶鋼を取MK 出
鋼しつつ、フェロシリコン1フエロマンガン・アルミニ
ウム等を添加し、クロム以外の合曾元素を目標成分に調
整する。この場合、転炉スラグを除去し、転炉スラグか
らの復燐を防止することによシ、溶鋼の低燐化が達成で
きる。
Next, the implementation method will be explained. Carbon smelted in converter 0
.. While tapping the molten steel containing 30% or less phosphorus and 30 ppm or less, ferrosilicon, ferromanganese, aluminum, etc. are added to adjust the combined elements other than chromium to the target composition. In this case, by removing the converter slag and preventing rephosphorization from the converter slag, it is possible to reduce the phosphorus content of the molten steel.

次に、レードルファーネス等の脱硫装置i”を用い、硫
黄を20 ppm以下になるまで除去する。このように
して、低燐、低値になった溶鋼を真空脱ガス装置でクロ
ム添加処理と脱水素処理を行う。脱水素処理は通常の真
空脱ガス処理方法と同じであるが、クロムを添加するた
め、下記のような操作を同時に行う。つまり1.可溶性
アルミニウムを0.050比以上に調整した溶鋼にアル
ゴンガスを用い5震以下のクロム酸化物を溶鋼中に吹き
込む操作を追加する。このようにすれば、可溶性アルミ
ニウムでクロム酸化物が還元され、溶鋼中への金属クロ
ムの添加が可能となる。
Next, sulfur is removed to 20 ppm or less using a desulfurization device such as a ladle furnace.The molten steel that has become low in phosphorus and has a low value is then subjected to chromium addition treatment and dehydration using a vacuum degassing device. Perform elementary treatment. Dehydrogenation treatment is the same as the normal vacuum degassing treatment method, but in order to add chromium, the following operations are performed at the same time: 1. Adjust soluble aluminum to a ratio of 0.050 or higher An additional operation is added to the molten steel in which chromium oxide with a concentration of 5 or less is injected into the molten steel using argon gas.In this way, the chromium oxide is reduced with soluble aluminum, making it possible to add metallic chromium to the molten steel. becomes.

溶鋼中への激化クロムの吹き込み方法としては、第3図
(a)に示したように、取鍋1に入れた溶鋼2の中に真
空脱ガス装置の上昇管4と下降管3を浸漬する。その後
、真空槽5を減圧し、環流ガス吹き込み羽口6からアル
ゴンガスを吹き込むことにより、溶鋼2を真空槽5に導
き脱ガスをする。この時、真空槽底部に設iたクロム酸
化物吹き込み羽ロフからアルゴンガスでクロム酸化物を
吹き込む方法でも良く。又、第3図(′bjに示したよ
うに、取鍋1に入れた溶鋼2の中に真空脱ガス装置の上
昇管4と下降管3を浸漬し、その後、真空槽5を減圧し
、環流ガス吹き込み羽口6からアルゴンガス全欧き込む
ことによシ、溶鋼2を真空槽5に導き脱ガスをする。こ
の時、取鍋1内の溶鋼2に浸漬したクロム酸化物吹き込
みランス8からアルゴンガスを用いて、クロムば化物を
吹き込む方法でも良い。或いは、第3図(C)に示した
ように、溶鋼2を入れた取鍋1にクロム酸化物吹き込み
ランス9を浸漬して、クロム酸化物をアルゴンカスで吹
き込んでも良い。以上のような処理全行えば低燐クロム
含有銅の溶製が可能になる。
As shown in FIG. 3(a), the method for injecting intensified chromium into molten steel is to immerse the riser pipe 4 and downfall pipe 3 of the vacuum degasser into the molten steel 2 placed in the ladle 1. . Thereafter, the vacuum chamber 5 is depressurized and argon gas is blown into the reflux gas blowing tuyere 6 to guide the molten steel 2 into the vacuum chamber 5 and degas it. At this time, the chromium oxide may be blown in with argon gas from a chromium oxide blowing vane provided at the bottom of the vacuum chamber. In addition, as shown in FIG. 3 ('bj), the rising pipe 4 and the descending pipe 3 of the vacuum degassing device are immersed in the molten steel 2 placed in the ladle 1, and then the vacuum chamber 5 is depressurized. The molten steel 2 is introduced into the vacuum chamber 5 and degassed by injecting argon gas all through the reflux gas blowing tuyeres 6. At this time, the chromium oxide blowing lance 8 immersed in the molten steel 2 in the ladle 1 Alternatively, as shown in FIG. 3(C), a chromium oxide injection lance 9 is immersed in a ladle 1 containing molten steel 2. Chromium oxide may be blown in with an argon gas.If all of the above treatments are carried out, copper with low phosphorous and chromium content can be melted.

(実施例) 実施例1は溶鋼温度1650℃、炭素0.1o%、シI
J コア 0.25%、マンガニ10.95%、燐0.
0015%、硫黄0.0015%、可溶性アルミニウム
0.055〜0.065%を確保した溶鋼150tを真
空脱ガス装置で真空度1 torr以下で脱ガス処理し
つつ、純度98%のクロム酸化物1000 hをアルゴ
ンガスで真壁脱ガス装置の下部槽に10分間で吹き込ん
だ場合である。溶鋼中のクロムは0.45%上昇し、歩
留は82%でのった。又、燐の上昇は見られなかった。
(Example) In Example 1, the molten steel temperature was 1650°C, carbon was 0.1%, and SiI
J Core 0.25%, Mangani 10.95%, Phosphorus 0.
150 tons of molten steel with 0.0015% sulfur, 0.0015% sulfur, and 0.055 to 0.065% soluble aluminum are degassed using a vacuum degassing device at a vacuum level of 1 torr or less, and chromium oxide 1000% with a purity of 98% is extracted. This is the case where argon gas was blown into the lower tank of the Makabe degassing device for 10 minutes. Chromium in the molten steel increased by 0.45%, and the yield was 82%. Also, no increase in phosphorus was observed.

尚、真空脱ガス装置の上部よシ、アルミニウムを溶鋼内
に添加し、可溶性アルミニウム含有11wcを確保した
Incidentally, aluminum was added to the molten steel in the upper part of the vacuum degasser to ensure a soluble aluminum content of 11wc.

実施例2は溶鋼温度1650℃、炭素0.10%、シリ
コン0.25%、マンガン0.95%、燐0.0015
%、硫黄0.0015%、可溶性アルミニウム0.05
5%〜0.065%を確保した溶vs150tを真空脱
ガス装置で真空度1 torr以下で脱ガス処理しつつ
、純度98%のクロム酸化物4500/19J−アルゴ
ンガスで真空脱ガス装置の下部槽に10分間で吹き込ん
だ場合である。溶鋼中のクロムは2.0%上昇し、歩留
は81%セあった。又、燐の上昇は見られなかった。尚
、真空脱ガス装置の上部より、アルミニウムを溶鋼内に
添加し、可溶性アルミニウム含有量を確保した。
Example 2 has a molten steel temperature of 1650°C, carbon 0.10%, silicon 0.25%, manganese 0.95%, and phosphorus 0.0015%.
%, sulfur 0.0015%, soluble aluminum 0.05
While degassing the molten vs150t with a concentration of 5% to 0.065% at a vacuum level of 1 torr or less using a vacuum degassing device, chromium oxide with a purity of 98% is removed from the bottom of the vacuum degassing device using 4500/19J-argon gas. This is the case where the water was blown into the tank for 10 minutes. Chromium in the molten steel increased by 2.0%, and the yield was 81%. Also, no increase in phosphorus was observed. Note that aluminum was added to the molten steel from the top of the vacuum degasser to ensure the soluble aluminum content.

比較例は溶鋼温度1680℃、炭素0.10%、シリコ
ン0.25%、マンガン0.959F;、燐0.001
5%、硫黄0.0015%、可溶性アルミニウム0.0
552の溶鋼150tを真空脱ガス装置で脱ガス処理し
つつ、クロム含有1t’75%のフェロクロム4200
Kyk真空檜内の上部から添加した。溶鋼中のクロムは
2−Oy、上昇し、歩留は95%であった。又、燐をo
o05%と大きく上昇した。    ゛以上のごとく、
本発明方法を溶鋼処理に用いることにより、容易に低燐
含有クロム鋼の溶製が可能となった。
Comparative example is molten steel temperature 1680℃, carbon 0.10%, silicon 0.25%, manganese 0.959F; phosphorus 0.001
5%, sulfur 0.0015%, soluble aluminum 0.0
While degassing 150 tons of molten steel of No. 552 using a vacuum degassing device, 1 tons of ferrochrome 4200 with a chromium content of 75% was processed.
It was added from the top inside the Kyk vacuum hinoki. The chromium in the molten steel increased by 2-Oy, and the yield was 95%. Also, phosphorus
It increased significantly to 05%.゛As above,
By using the method of the present invention for processing molten steel, it has become possible to easily produce chromium steel with low phosphorus content.

(発明の効果〕 本発明によれば、従来の低燐含有クロム鋼の溶製方法と
比較して、脱燐処理工程が省略でき、且つ10分間とい
う通常の脱ガス処理時間内でクロムが添加することが可
能になった。このため、全体の溶鋼処理時間が短縮され
、溶鋼の温度降下が小さくなり、取鏑或いは脱ガス設備
の耐火物の溶損が少なくなるため操業上の支障をも防止
可能となった。又、高価な蛍属クロムを用いなくても、
例えば、精製したクロム鉱石等を使用しても、低燐クロ
ム含有銅の溶製が可能となった。このように、本発明に
よnば、従来方法と比較して容易かつ、確実に低燐クロ
ム含有銅が溶製できる等の優男1図はクロム酸化物の還
元におよぼす可溶性アルミニウム含有量の影響を示す図
、第2図はクロムば化物の還元におよぼすクロム酸化物
直径の影響を示す図、第3図(a)、第3図+1)lは
RH真空脱ガス装置でのクロムの酸化物の添加方法の概
略図第3図(c)は上吹き粉体吹き込み装置でのクロム
酸化物の添加方法の概略iである。
(Effects of the Invention) According to the present invention, compared to the conventional melting method for low phosphorus-containing chromium steel, the dephosphorization process can be omitted, and chromium can be added within the normal degassing time of 10 minutes. As a result, the overall molten steel processing time is shortened, the temperature drop of the molten steel is reduced, and there is less erosion of refractories in the take-off or degassing equipment, so there are no operational hindrances. It is now possible to prevent this.Also, it can be prevented without using expensive fluorescent chromium.
For example, it has become possible to melt copper with low phosphorus and chromium content even by using purified chromium ore. As described above, according to the present invention, copper containing low phosphorous and chromium can be melted easily and reliably compared to conventional methods. Figure 2 is a diagram showing the effect of chromium oxide diameter on the reduction of chromium oxide, Figure 3 (a), Figure 3+1) l is a diagram showing the effect of chromium oxide diameter on the reduction of chromium oxide, Figure 3(c) is a schematic diagram of the method of adding chromium oxide using a top blowing powder blowing device.

1・・・・・・取鍋 2・・・・・・溶鋼 3・・・・・・下降管 4・・・・・・上昇管 5・・・・・・真空槽 6・・・・・・環流ガス吹き込み羽ロ ア・・・・・・クロム酸化物吹き込み羽口8.9・・・
・・クロムは化物吹き込みランス出 願 人 新日本製
鐵株式会社 第1図 0   .0,05    0.to     O,+
5    02゜呵寿セL7 Ivミ;つ4(7’、) 第2凶
1... Ladle 2... Molten steel 3... Descending pipe 4... Rising pipe 5... Vacuum chamber 6...・Recirculation gas blowing vane lower・・・Chromium oxide blowing tuyere 8.9・・・
...Chromium is a chemical injection lance Applicant: Nippon Steel Corporation Figure 1 0. 0,05 0. to O,+
5 02゜呵juse L7 Ivmi;tsu4 (7',) 2nd evil

Claims (1)

【特許請求の範囲】[Claims] 炭素が0.30%以下、燐100ppm以下、可溶性ア
ルミニウムを0.050%以上含有する溶鋼中に、直径
5mm以下のクロム酸化物を不活性ガスを用いて吹き込
むことを特徴とする低燐クロム含有銅の溶製方法。
Low phosphorus chromium content characterized by blowing chromium oxide with a diameter of 5 mm or less into molten steel containing 0.30% or less carbon, 100 ppm or less phosphorus, and 0.050% or more soluble aluminum using an inert gas. Copper melting method.
JP25002186A 1986-10-21 1986-10-21 Method for producing steel containing low phosphorous and chromium Pending JPS63105915A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25002186A JPS63105915A (en) 1986-10-21 1986-10-21 Method for producing steel containing low phosphorous and chromium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25002186A JPS63105915A (en) 1986-10-21 1986-10-21 Method for producing steel containing low phosphorous and chromium

Publications (1)

Publication Number Publication Date
JPS63105915A true JPS63105915A (en) 1988-05-11

Family

ID=17201665

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25002186A Pending JPS63105915A (en) 1986-10-21 1986-10-21 Method for producing steel containing low phosphorous and chromium

Country Status (1)

Country Link
JP (1) JPS63105915A (en)

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