JPH02232313A - Dephosphorizing agent for molten steel - Google Patents

Dephosphorizing agent for molten steel

Info

Publication number
JPH02232313A
JPH02232313A JP1052086A JP5208689A JPH02232313A JP H02232313 A JPH02232313 A JP H02232313A JP 1052086 A JP1052086 A JP 1052086A JP 5208689 A JP5208689 A JP 5208689A JP H02232313 A JPH02232313 A JP H02232313A
Authority
JP
Japan
Prior art keywords
molten steel
dephosphorizing agent
compsn
weight
dephosphorizing
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
JP1052086A
Other languages
Japanese (ja)
Inventor
Tomio Tsuchiya
土谷 登美夫
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.)
TAIYO GIKEN KOGYO KK
Original Assignee
TAIYO GIKEN KOGYO KK
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 TAIYO GIKEN KOGYO KK filed Critical TAIYO GIKEN KOGYO KK
Priority to JP1052086A priority Critical patent/JPH02232313A/en
Publication of JPH02232313A publication Critical patent/JPH02232313A/en
Pending legal-status Critical Current

Links

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

  • Treatment Of Steel In Its Molten State (AREA)

Abstract

PURPOSE:To obtain the dephosphorizing agent for a molten steel of a low cost which has good reaction efficiency, is nonpollutive and does not generate the damages of refractories, environmental pollution, etc., by premelting a compsn. having a specific compsn. consisting of calcium aluminate and iron oxide. CONSTITUTION:The calcium aluminate of the compsn. consisting of the calcium aluminate and the iron oxide or the entire part of the compsn. premelted or sintered. Further, this compsn. is composed of 30 to 50wt.% CaO, 25 to 45% Al2O3, 10 to 30% FeO+Fe2O3, <=3% SiO2, and the balance inevitable impurities. The above-mentioned iron oxide is partly substd. with chromium oxide to make 5 to 15% Cr2O3 and 0.1 to 10% FeO+Fe2O3 at need. The dephosphorizing agent for the molten steel which does not contain harmful, corrosive, costly and fume- generating components and slags off easily is obtd. in this way.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は溶鋼の精錬IC使用すb脱りん剤でろって,と
くに酸化脱りん法に供せられる脱りん剤に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a dephosphorizing agent used in an IC for refining molten steel, and particularly to a dephosphorizing agent used in an oxidative dephosphorizing method.

(従来の技術) 鋼に対してクんは一般に有害元素でろって,機械的性質
,溶接性,鍛接性に悪影響を及ぼす。また,とくに含ク
ロム鋼におっては応力腐食割れの原因ともなるものであ
る。
(Prior art) Metals are generally harmful elements to steel, and have a negative effect on mechanical properties, weldability, and forge weldability. It also causes stress corrosion cracking, especially in chromium-containing steel.

近年.鋼材に対する高品質化への要求が高まるにともな
って,そのより以上の低りん化が強く求められ,溶鋼の
精練における脱りん法も従来のCaO系スラグによる酸
化精錬に対して多くの技術的改良が加えられている。
recent years. As the demand for higher quality steel materials increases, there is a strong demand for even lower phosphorus, and many technological improvements have been made to the dephosphorization method in molten steel refining compared to the conventional oxidation refining using CaO-based slag. has been added.

溶鋼の脱りん処理にあたり,脱りん剤として種々のフラ
ックスが提唱されているが,脱りん反応の形態によって
還元脱りん剤と酸化脱りん剤とに区分される。また.酸
化脱りん剤に対しては,とくに含クロム鋼の場合にクロ
ムの選択酸化にょる減耗を避けて有効に脱りん反応を進
行させるものでおることが主眼とされ九。
Various fluxes have been proposed as dephosphorizing agents for dephosphorizing molten steel, but they are classified into reductive dephosphorizing agents and oxidizing dephosphorizing agents depending on the form of the dephosphorizing reaction. Also. Regarding oxidative dephosphorizing agents, the main aim is to avoid the depletion of chromium due to selective oxidation, especially in the case of chromium-containing steel, and to effectively promote the dephosphorizing reaction9.

従来提唱されている脱りん剤をあげれば次のとおりであ
る。
The dephosphorizing agents that have been proposed so far are as follows.

(1)  還元脱りん剤:Ca−CaP2系, CaC
2−CaF2系。
(1) Reduction dephosphorizing agent: Ca-CaP2 system, CaC
2-CaF2 system.

(2)  酸化脱りん剤: (Cab, Bad, N
a2CO3,Li2CO3)一ハロゲン化物系。
(2) Oxidative dephosphorizer: (Cab, Bad, N
a2CO3, Li2CO3) monohalide system.

(発明が解決しようとする課題) 前項にあげた従来の脱リん剤については、それぞれ次の
ような課題が指摘される。
(Problems to be Solved by the Invention) The following problems have been pointed out with respect to the conventional dephosphorizing agents listed in the previous section.

(1)還元脱りん剤:脱りん後スラグの無害化処理を必
要とする。さらに,Ca系においてはCaの蒸発による
効率低下,もしくはEARを必要とすることによる高コ
スト化が1ま7’(CaC2系においては耐火物の損傷
がめげられる。
(1) Reduction dephosphorizing agent: Requires detoxifying treatment of slag after dephosphorization. Furthermore, in the Ca system, efficiency decreases due to evaporation of Ca or increases in cost due to the need for EAR (in the CaC2 system, damage to the refractory is caused).

(2)  酸化脱りん剤:ハロゲ/化物による耐火物の
損傷.還境汚染のほか, BaO,LICO3系におけ
る高コス}化, Na2COl系におけるヒュームの発
生があげられる。
(2) Oxidative dephosphorizer: Damage to refractories due to halogens/compounds. In addition to environmental pollution, the increase in cost in BaO and LICO3 systems and the generation of fumes in Na2COl systems are also cited.

これらの課題に対して,本発明は脱りん後スラグの無害
化処理を必要とせず,耐火物の損傷,環境汚染.高コス
ト化を解決するものとして新規な脱りん剤を提供するも
のである。
In order to solve these problems, the present invention eliminates the need to detoxify the slag after dephosphorization, and reduces the risk of damage to refractories and environmental pollution. The present invention provides a new dephosphorizing agent to solve the problem of high costs.

(課題を解決するための手段) 本発明は,カルシウムアルミネートと酸化鉄より成る組
成物であって,カルシウムアルミネートもしくは組成物
全体がブリメルトされ,かつCaO30−50重量%,
 AlzOx 25−45重量チ.FeO+Fe203
 1 Q − 3 0重量%, Si02 3重量チ以
下,残部がその他の避けられない不純物よp成ることを
特徴とする溶鋼の脱りん剤を第一発明とするものである
(Means for Solving the Problems) The present invention provides a composition comprising calcium aluminate and iron oxide, in which the calcium aluminate or the entire composition is brimelted, and 30-50% by weight of CaO,
AlzOx 25-45 weight chi. FeO+Fe203
The first invention is a dephosphorizing agent for molten steel, characterized in that it consists of 0% by weight of 1Q-3, 3% by weight of Si02 or less, and the balance consisting of other unavoidable impurities.

しかして.第二発明として前記の酸化鉄に代えて酸化ク
Olhとし,  FeO+Fe203 1 0 − 3
 0重量%iて代えてCr203 5 − 1 5重量
チ及びFeO+Fe20301〜10重量チとすること
を特徴とする溶鋼の脱りん剤を提供するものである。
However. As a second invention, in place of the above-mentioned iron oxide, oxidized oxide Olh is used, FeO+Fe203 1 0 - 3
The present invention provides a dephosphorizing agent for molten steel characterized in that 0% by weight i is replaced with 5% by weight of Cr203 and 1 to 10% by weight of FeO+Fe2030.

さらに,第三発明として,前記のブリメルトに代えて焼
結されることを特徴とする溶鋼の脱りん剤を提供するも
のである。
Furthermore, as a third invention, there is provided a dephosphorizing agent for molten steel, characterized in that it is sintered instead of the Brimelt described above.

ここに,カルシウムアルミネートは12cao・7Al
2CNの共晶組成を有し, CaO−)J20コ系では
最低の融点(約L385℃》をもつものである。
Here, calcium aluminate is 12cao・7Al
It has a eutectic composition of 2CN and has the lowest melting point (approximately 385°C) in the CaO-)J20 series.

CaO系フラックスに対しては脱りん反応を促進させる
ために,融点降下・滓化促進剤としてCaF2が有効で
あり多用されているが,反面,耐火物を損傷し,環境を
汚染する要因ともなるので本発明ではCaF2に代えて
人l203を選択した。これは,AltosがCaO 
i’il:対して十分な融点降下・滓化促進能を有し.
脱りん反応の促進にM用であるとの知見による。
For CaO-based fluxes, CaF2 is effective and frequently used as a melting point lowering and slag accelerator to promote the dephosphorization reaction, but on the other hand, it can damage refractories and pollute the environment. Therefore, in the present invention, human 1203 was selected instead of CaF2. This means that Altos is CaO
i'il: has sufficient ability to lower the melting point and promote sludge formation.
This is based on the knowledge that M is used to promote the dephosphorization reaction.

また.ブリメルト品とし友のは組成的に均質なものとし
,ひいては溶鋼との接触において溶融・滓化を容易にす
るためである。プリメルトについては.カルシウムアル
ミネートのみをその対象とするも,酸化鉄もしくは酸化
クロムとの組成物全体とするもいずれでもよい。
Also. Brimelt products are made to be homogeneous in composition, which in turn facilitates melting and slag formation upon contact with molten steel. Regarding Primelt. The target may be either only calcium aluminate or the entire composition with iron oxide or chromium oxide.

第一発明における酸化鉄,第二発明における酸化クロム
はともに酸化脱りんに際して酸化剤として作用せしめる
ものである。酸化鉄として便用し得るのは,製鉄工場か
ら容易に入手できるミルスケールが好適でるり,他に弁
柄も適品である。酸化クロムとしてはクロマイトサント
−クロム鉱石などを使用する。クロマイトサンドについ
ては,鋳造工場で使用後の廃砂を利用するのもよい。
Both the iron oxide in the first invention and the chromium oxide in the second invention act as an oxidizing agent during oxidative dephosphorization. Mill scale, which can be easily obtained from iron factories, is suitable as iron oxide, and Bengara is also suitable. As the chromium oxide, chromite sant-chromium ore is used. As for chromite sand, it is also a good idea to use waste sand from a foundry.

ここにおいて,酸化鉄は含クロム鋼に対してはりんより
もクロムの優先的酸化剤として作用するので.この場合
は酸化クロムを用いるものとする。
Here, iron oxide acts as a preferential oxidizing agent for chromium rather than phosphorus for chromium-containing steel. In this case, chromium oxide shall be used.

すなわち,本発明の脱りん剤について,第二発明は含ク
ロム鋼用とし,第一発明はその他の炭素鋼,合金鋼用と
するものである。
That is, regarding the dephosphorizing agent of the present invention, the second invention is used for chromium-containing steel, and the first invention is used for other carbon steels and alloy steels.

5〜15重量チであって,この範囲を超えるときは反応
過多となり,未満では過少となってともに本発明の目的
を達し得ない。なお.第二発明におけるFeO+Fe2
0xは酸化剤原料から混入するもので避けられない成分
である。
If the amount is 5 to 15% by weight, if it exceeds this range, the reaction will be excessive, and if it is less than this, the reaction will be too small, and the object of the present invention cannot be achieved. In addition. FeO+Fe2 in the second invention
0x is an unavoidable component that is mixed in from the oxidizing agent raw material.

Si02も配合原料からの混入成分であるが.酸性成分
であるから滓の塩基度低下による脱りん反応の阻害を防
止する几め3重量チ以下とすることが必要でらる。
Si02 is also a mixed component from the blended raw materials. Since it is an acidic component, it is necessary to reduce the amount to 3% by weight or less to prevent inhibition of the dephosphorization reaction due to a decrease in the basicity of the slag.

CaOとAI!2 0 3の特定範囲については,カル
シウムアルミネートにおいて基本的なC a O/A.
.l 2 0 3の組成比は1/1であるから,プリメ
ルトもしくは焼結における原料歩留.酸化剤原料からの
ビノクアップを考慮するとき.適量範囲はCaO 3 
0〜50重量% , AJ203 2 5〜45重量チ
となる。
CaO and AI! For the specific range of 203, the basic C a O/A.
.. Since the composition ratio of l203 is 1/1, the raw material yield in premelt or sintering is low. When considering vinyl-up from oxidizer raw materials. The appropriate amount range is CaO 3
0 to 50% by weight, AJ203 2 5 to 45% by weight.

この範囲を超えるときも,また未満のときも.ともに融
点が上昇して脱りんの反応速度が低下するから好ましく
ない。
Both above and below this range. Both are undesirable because the melting point increases and the dephosphorization reaction rate decreases.

なお,第三発明において焼結は融点直下で行われ,第一
,第二発明によるものに準じて本発明の目的達成のため
に使用される。
In addition, in the third invention, sintering is performed just below the melting point, and is used to achieve the object of the present invention in the same manner as in the first and second inventions.

(作 用) 本発明による脱りん剤は,ブリメルト品であるカルシウ
ムアルミネートと酸化剤とを適当粒度に砕粒・混合し次
ものとして.炉中.炉外の別なく溶鋼の脱りん精錬に供
せられる。
(Function) The dephosphorizing agent according to the present invention is prepared by crushing and mixing calcium aluminate, which is a Brimelt product, and an oxidizing agent to an appropriate particle size. Inside the furnace. It is used for dephosphorization of molten steel, regardless of whether it is outside the furnace.

従来のCaO系脱りん剤では.酸化剤を含むものにあっ
てはスラグの固化を避け,溶化を促進するものとしてハ
ロゲン化物を含むものが知られているが,本発明の脱り
ん剤はこれをカルシウムアルミ不−トとすることにより
・・ロゲン化物を全く含まないものとしたのでちる。
With conventional CaO-based dephosphorizing agents. Among those containing oxidizing agents, those containing halides are known to avoid solidification of slag and promote solubilization, but the dephosphorizing agent of the present invention uses calcium aluminum inert instead of halides. As a result, it contains no rogens at all.

すなわち,本発明によれば,脱りん剤は速かに滓化して
酸化剤による鋼浴中ジんの酸化を進行させてP205と
し.さらにCaOとの反応によりきわめて安定な3Ca
O−P205を形成してスラグとともに除去し得るもの
となるのである。
That is, according to the present invention, the dephosphorizing agent quickly turns into slag, and the oxidizing agent progresses the oxidation of the slag in the steel bath, resulting in P205. Furthermore, 3Ca is extremely stable due to the reaction with CaO.
This allows O-P205 to be formed and removed together with the slag.

酸化剤として用いる酸化鉄はFeOの供給源であるから
,含クロム鋼K−あってはりんよクもクロムを優先的に
酸化することとな,b.LAがって,含クロム鋼に対し
ては酸化クロムを酸化剤としたことは既述のとおりであ
る。
Since iron oxide used as an oxidizing agent is a source of FeO, chromium-containing steel K- and Rin-yoku also preferentially oxidize chromium, b. As mentioned above, chromium oxide was used as the oxidizing agent for chromium-containing steel in LA.

なお,本発明の脱9ん剤の関与する脱りん反応式を次に
示す。
The dephosphorization reaction formula involving the dephosphorization agent of the present invention is shown below.

2ヱ + 50  =  P20S 3 (CaO)+ 2E + 5Q−+(Ca sPJ
)+ 4C4 = Ca 3(POi )i(実施例) 本発明の実施例を次に示す。
2ヱ + 50 = P20S 3 (CaO) + 2E + 5Q-+ (Ca sPJ
)+4C4=Ca3(POi)i (Example) Examples of the present invention are shown below.

実施例1 等量の石灰石とボーキサイトを溶解炉に装入し1500
℃以上の温度でカルシウムアルミネートを溶製した。こ
れを3』以下の粒径となるように粉砕したものに対して
.同様粒度に調整したミルスケールを混合比4:1とな
るように加えて十分に混合し,第1表に示す組成の脱り
ん剤体)を得た。
Example 1 Equal amounts of limestone and bauxite were charged into a melting furnace and the melting temperature was 1500.
Calcium aluminate was melted at temperatures above ℃. This is crushed to a particle size of 3'' or less. Mill scale adjusted to the same particle size was added at a mixing ratio of 4:1 and thoroughly mixed to obtain a dephosphorizing agent having the composition shown in Table 1.

これを高周波誘導炉で溶解し7t−lionの0.05
チC鋼に10〜散布添加して脱りん処理を行った。
This was melted in a high frequency induction furnace to produce 7t-lion of 0.05
A dephosphorization treatment was carried out by adding 10 to 10% of the mixture to C steel.

添加時の鋼浴温度は1600℃であク.投入後友。The steel bath temperature at the time of addition was 1600℃. Friend after input.

実施例2 これ七粒径3N1以下に粉砕後電弧炉で溶解した3ot
onの3 % Cr−1%C鋼浴に210Kft炉中投
入し,脱りん処理を行った。投入時の鋼浴温度はL50
0℃であり.鋼浴中のりん濃度に処理前の第 1 表(
重量チ) その他の実施の態様として,本発明の脱りん剤をキャリ
アカスな介して浴中に吹込んだり,コアードワイヤの形
態で浸漬処理してもよい。
Example 2 3 oz of this was crushed to a particle size of 3N1 or less and then melted in an electric arc furnace.
The sample was placed in a 210 Kft furnace in a 3% Cr-1% C steel bath for dephosphorization. The steel bath temperature at the time of charging is L50.
It is 0℃. Table 1 shows the phosphorus concentration in the steel bath before treatment (
In other embodiments, the dephosphorizing agent of the present invention may be blown into the bath through a carrier cassette, or may be immersed in the form of a cored wire.

(発明の効果) 本発明の脱りん剤は次のような効果をも友らすものでち
る。
(Effects of the Invention) The dephosphorizing agent of the present invention also has the following effects.

(11  ブリメルトもしくは焼結されたカルシウムア
ルミネートが主成分であって,鋼よりも低融点であるか
ら脱りんの反応効率が良好でるる。
(11) The main component is brimelt or sintered calcium aluminate, which has a lower melting point than steel, so the dephosphorization reaction efficiency is good.

i2l  C aO−Al 2 0 3系でめる九め,
スラグの塩基度調整が容易であり1脱りん反応の促進に
有効でおる。
i2l CaO-Al 2 0 3 system,
It is easy to adjust the basicity of the slag and is effective in promoting the dephosphorization reaction.

(3)  ハロゲン化物を含まないため.それによる耐
火物の損傷と環境汚染を避けられる。
(3) Because it does not contain halides. This can avoid damage to refractories and environmental pollution.

(4)鋼浴添加時に発煙,発塵,臭気カスの発生がない
(4) No smoke, dust, or odor residue is generated when adding steel to the bath.

(5)生成スラグは無害化処理を必要としない。(5) The generated slag does not require detoxification treatment.

(6)処理反応時の吸熱が小さいためと一トロスが少な
い。
(6) Because the endotherm during the treatment reaction is small, the amount of loss is small.

(力 吸湿性ではないkめ保管管理が容易である。(Since it is not hygroscopic, storage management is easy.

(8)脱りん処理を低コスト化し得る。(8) The cost of dephosphorization treatment can be reduced.

以上より本発明の脱りん剤は,従来の課題を解決するも
のとして高品質の低りん鋼の製造に大いに寄与するもの
である。
As described above, the dephosphorizing agent of the present invention solves the conventional problems and greatly contributes to the production of high quality low phosphorus steel.

特許出願人 太洋技研工業株式会社Patent applicant Taiyo Giken Kogyo Co., Ltd.

Claims (1)

【特許請求の範囲】 1、カルシウムアルミネートと酸化鉄より成る組成物で
あって、カルシウムアルミネートもしくは組成物全体が
プリメルトされ、かつCaO30〜50重量%、Al_
2O_325〜45重量%、FeO+Fe_2O_31
0〜30重量%、SiO_23重量%以下、残部がその
他の避けられない不純物より成ることを特徴とする溶鋼
の脱りん剤。 2、請求項1記載の溶鋼の脱りん剤において、酸化鉄に
代えて酸化クロムとし、FeO+Fe_2O_310〜
30重量%に代えてCr_2O_35〜15重量%及び
FeO+Fe_2O_30.1〜10重量%とすること
を特徴とする溶鋼の脱りん剤 3、請求項1又は2記載の溶鋼の脱りん剤において、プ
リメルトに代えて焼結されることを特徴とする溶鋼の脱
りん剤。
[Claims] 1. A composition consisting of calcium aluminate and iron oxide, wherein the calcium aluminate or the entire composition is premelted, and 30 to 50% by weight of CaO, Al_
2O_325-45% by weight, FeO+Fe_2O_31
A dephosphorizing agent for molten steel, characterized in that it contains 0 to 30% by weight, SiO_23% by weight or less, and the remainder consists of other unavoidable impurities. 2. In the dephosphorizing agent for molten steel according to claim 1, chromium oxide is used instead of iron oxide, and FeO+Fe_2O_310~
A molten steel dephosphorizing agent 3 characterized in that Cr_2O_35 to 15% by weight and FeO+Fe_2O_30.1 to 10% by weight are used instead of 30% by weight, in the molten steel dephosphorizing agent according to claim 1 or 2, in place of premelt. A dephosphorizing agent for molten steel, which is characterized by being sintered.
JP1052086A 1989-03-06 1989-03-06 Dephosphorizing agent for molten steel Pending JPH02232313A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1052086A JPH02232313A (en) 1989-03-06 1989-03-06 Dephosphorizing agent for molten steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1052086A JPH02232313A (en) 1989-03-06 1989-03-06 Dephosphorizing agent for molten steel

Publications (1)

Publication Number Publication Date
JPH02232313A true JPH02232313A (en) 1990-09-14

Family

ID=12905018

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1052086A Pending JPH02232313A (en) 1989-03-06 1989-03-06 Dephosphorizing agent for molten steel

Country Status (1)

Country Link
JP (1) JPH02232313A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100415925B1 (en) * 1998-12-30 2004-03-26 주식회사 포스코 Calcium Aluminate Additives
CN103060522A (en) * 2013-02-08 2013-04-24 武钢集团昆明钢铁股份有限公司 Slag forming agent for dephosphorization of medium-high-phosphorus semisteel and preparation method of slag forming agent
CN103060527A (en) * 2013-02-04 2013-04-24 山西太钢不锈钢股份有限公司 Slagging method of axle steel LF (Ladle Refining) furnace
JP2014031562A (en) * 2012-08-06 2014-02-20 Nippon Steel & Sumitomo Metal Dephosphorization processing method of hot pig iron
JP2014037570A (en) * 2012-08-14 2014-02-27 Nippon Steel & Sumitomo Metal High speed blowing method for converter
CN104451034A (en) * 2015-01-06 2015-03-25 攀钢集团攀枝花钢铁研究院有限公司 Semisteel desulfuration dephosphorization agent and preparing method and application thereof
CN104451033A (en) * 2015-01-06 2015-03-25 攀钢集团攀枝花钢铁研究院有限公司 Semisteel desulfuration dephosphorization agents and preparing method and application thereof
CN104480253A (en) * 2015-01-06 2015-04-01 攀钢集团攀枝花钢铁研究院有限公司 Dephosphorization and desulfurization agent for semi-steel and preparation method and application thereof
WO2017119392A1 (en) * 2016-01-05 2017-07-13 新日鐵住金株式会社 Molten iron dephosphorizing agent, refining agent, and dephosphorization method

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100415925B1 (en) * 1998-12-30 2004-03-26 주식회사 포스코 Calcium Aluminate Additives
JP2014031562A (en) * 2012-08-06 2014-02-20 Nippon Steel & Sumitomo Metal Dephosphorization processing method of hot pig iron
JP2014037570A (en) * 2012-08-14 2014-02-27 Nippon Steel & Sumitomo Metal High speed blowing method for converter
CN103060527A (en) * 2013-02-04 2013-04-24 山西太钢不锈钢股份有限公司 Slagging method of axle steel LF (Ladle Refining) furnace
CN103060522A (en) * 2013-02-08 2013-04-24 武钢集团昆明钢铁股份有限公司 Slag forming agent for dephosphorization of medium-high-phosphorus semisteel and preparation method of slag forming agent
CN104451034A (en) * 2015-01-06 2015-03-25 攀钢集团攀枝花钢铁研究院有限公司 Semisteel desulfuration dephosphorization agent and preparing method and application thereof
CN104451033A (en) * 2015-01-06 2015-03-25 攀钢集团攀枝花钢铁研究院有限公司 Semisteel desulfuration dephosphorization agents and preparing method and application thereof
CN104480253A (en) * 2015-01-06 2015-04-01 攀钢集团攀枝花钢铁研究院有限公司 Dephosphorization and desulfurization agent for semi-steel and preparation method and application thereof
WO2017119392A1 (en) * 2016-01-05 2017-07-13 新日鐵住金株式会社 Molten iron dephosphorizing agent, refining agent, and dephosphorization method
CN107849625A (en) * 2016-01-05 2018-03-27 新日铁住金株式会社 Dephosphorising agent, refining agent and the dephosphorization method of molten iron
JPWO2017119392A1 (en) * 2016-01-05 2018-04-05 新日鐵住金株式会社 Molten iron dephosphorizing agent, refining agent and dephosphorizing method

Similar Documents

Publication Publication Date Title
EP0523167A1 (en) Compositions and methods for synthesizing ladle slags, treating ladle slags, and coating refractory linings
JP3503176B2 (en) Hot metal dephosphorizer for injection
JPH02232313A (en) Dephosphorizing agent for molten steel
US4853034A (en) Method of ladle desulfurizing molten steel
JPH0246647B2 (en)
US5425797A (en) Blended charge for steel production
JP2013064179A (en) Method for preventing elution of hexavalent chromium in slag, and slag
JP2011246765A (en) Method of reduction-refining molten steel
JP4388845B2 (en) Detoxification method for chromium-containing steel slag
JP4304110B2 (en) Detoxification method for chromium-containing steel slag
JP3574690B2 (en) Hot metal desulfurization method
KR900007441B1 (en) Additive for preventing slag forming
KR930006640B1 (en) Dephosporus agent for preheat treatmenting of molten metal
JP2000044298A (en) Method for preventing powdering of reduction slag
JP2002275521A (en) Method for dephosphorizing molten high carbon steel
SU1104165A1 (en) Charge for obtaining synthetic slag
JP2002285217A (en) Dephosphorizing agent and desulfurizing agent for molten iron and molten steel
JP3297997B2 (en) Hot metal removal method
JP3177267B2 (en) Manufacturing method of iron-chromium alloy
RU2201970C2 (en) Method of making steel in high-power electric arc furnaces
JP2022027515A (en) Method for desulfurizing molten steel and desulfurization flux
JPS6212301B2 (en)
SU1122708A1 (en) Charge for producing synthetic slag
JPH10317035A (en) Desulphurization method of ferrous molten alloy, and desulphurizing agent
SU591514A1 (en) Slag-forming mix