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JPS626606B2 - - Google Patents
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JPS626606B2 - - Google Patents

Info

Publication number
JPS626606B2
JPS626606B2 JP57076043A JP7604382A JPS626606B2 JP S626606 B2 JPS626606 B2 JP S626606B2 JP 57076043 A JP57076043 A JP 57076043A JP 7604382 A JP7604382 A JP 7604382A JP S626606 B2 JPS626606 B2 JP S626606B2
Authority
JP
Japan
Prior art keywords
molten steel
filter
inclusions
clinker
lime
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.)
Expired
Application number
JP57076043A
Other languages
Japanese (ja)
Other versions
JPS58193306A (en
Inventor
Takateru Nomura
Kyomi Shio
Yoichi Yokoyama
Tsutomu Shimizu
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 JP7604382A priority Critical patent/JPS58193306A/en
Publication of JPS58193306A publication Critical patent/JPS58193306A/en
Publication of JPS626606B2 publication Critical patent/JPS626606B2/ja
Granted 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
    • C21C7/04Removing impurities by adding a treating agent

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Casting Support Devices, Ladles, And Melt Control Thereby (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Treatment Of Steel In Its Molten State (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は溶鋼中の非金属介在物、特に微細な
Al2O3系介在物の除去に用いるフイルターに関す
るものである。 溶鋼中に残留する硫黄、燐、酸素又は非金属介
在物は鋼の加工性並びに機械性に悪影響を与え
る。近年鋼材に要求される品質は次第に厳しくな
り、これらの不純物の少いいわゆるクリーンスチ
ールが求められている。これらの不純物を除去す
る在来の方法としては、溶銑、溶鋼にCaO,
CaF2,Na2CO3等の精錬剤(フラツクス)を添加
して脱硫、脱燐処理を行う方法が行なわれてい
る。また鋼中水素、窒素等の脱ガスについては
RH式、DH式等の直空脱ガス装置により処理がな
されている。さらに脱酸すなわち非金属介在物の
除去も溶鋼清浄化の重要なポイントである。特に
Al脱酸鋼の場合は脱酸生成物であるAl2O3が溶鋼
中に懸濁しこれが鋳片の品質を低下させる原因と
なる。通常、連続鋳造の場合はタンデイシユ内で
これらの非金属介在物を浮上分離して清浄な溶鋼
として鋳型に注入される。しかし50μ以下の非常
に微細なAl2O3介在物について鋼中からの浮上分
離が困難であり適切な除去技術が確立されていな
いのが現状である。 本発明者らは、非金属介在物の除去について
種々の試験を行つた結果この微細なAl2O3介在物
を除去する有効なフイルターを見出した。すなわ
ち石灰クリンカー単独からなるもしくは50wt%
以上の石灰クリンカーと残部がマグネシアクリン
カー又はドロマイトクリンカーからなる塩基性材
料で構成され多数の溶鋼通過孔を有する石灰質フ
イルターである。本発明者らは、種々の実験によ
り溶鋼と接触した石灰質耐火物が鋼中のAl2O3
結びつきやすく、それを吸収しやすいという知見
を得た。本発明はこの現象を積極的に利用したも
のであり、多数の溶鋼通過孔に溶鋼を弾通過させ
て接触チヤンスを多くして溶鋼中のAl2O3介在物
を吸収除去せしめる石灰質の介在物除去用フイル
ターである。 石灰と接触したAl2O3介在物は x・CaO+yAl2O3=xCaO・yAl2O3 なる反応により例えば3CaO・Al2O3,12CaO・
7Al2O3等のカルシウムアルミネートを容易に生
成して石灰質フイルター内へ吸収されることとな
る。 非金属介在物除去用フイルターの具備すべき特
性の一つとして溶鋼との反応によりそれ自身が介
在物起源となつてはならないことがあげられる。
酸性耐火物の場合は次式により鋼中Alと耐火物
主成分であるSiO2が反応しAl2O3を生成しやす
い。 4Al+3SiO2=2Al2O3+3Si これに対して本発明で用いる塩基性材料、なか
でも石灰CaOはそれ自身2500℃以上の高融点を有
するとともに解離酸素圧および蒸気圧が低く真空
中でも安定であり溶鋼に対しても最も安定な耐火
材料である。 フイルターの組成のうちCaOの占める割合は大
きいほどそれ自身が介在物源となりにくいととも
にAl2O3の反応性が良いことはいうまでもない。
CaOクリンカーの割合が50wt%以下の場合は
Al2O3との反応性が低下し介在物除去用が減少す
る恐れがある。 本発明者らはさらにフイルターの材質について
検討を加え、石灰または石灰―マグネシア(ドロ
マイト)の材質に1〜20wt%のCaCl2を添加する
ことによりさらに溶鋼中のAl2O3を吸着しやすい
ことを見出した。すなわち本発明のフイルターの
使用時には、予熱あるいは溶鋼の温度により
CaCl2の融点(772℃)以上に加熱されているた
めCaCl2は液相状態で存在する。そのため吸収し
たAl2O3系介在物をフイルターの内部へ移動させ
やすく吸収効果が大きくなるものと考える。
CaCl2の添加量を20wt%以下としたのは、それ以
上だと液相量が多くなりすぎ熱間での強度が低下
するため溶鋼による損耗が大きくなるからであ
る。第1図は石灰および石灰―CaCl2質耐火物を
タンデイシユ内の溶鋼中に浸漬したときのAl2O3
の吸収の分析例を示す図である。
The present invention deals with non-metallic inclusions in molten steel, especially fine particles.
This invention relates to a filter used to remove Al 2 O 3 based inclusions. Sulfur, phosphorus, oxygen, or nonmetallic inclusions remaining in molten steel adversely affect the workability and mechanical properties of steel. In recent years, the quality required for steel materials has become increasingly strict, and so-called clean steel with fewer impurities is in demand. Conventional methods for removing these impurities include adding CaO to hot metal and molten steel.
Desulfurization and dephosphorization treatments are carried out by adding refining agents (fluxes) such as CaF 2 and Na 2 CO 3 . Regarding degassing of hydrogen, nitrogen, etc. in steel,
Treatment is performed using direct air degassing equipment such as RH type and DH type. Furthermore, deoxidation, that is, removal of nonmetallic inclusions, is also an important point in cleaning molten steel. especially
In the case of Al-deoxidized steel, Al 2 O 3 , which is a deoxidation product, is suspended in the molten steel, which causes deterioration in the quality of the slab. Normally, in the case of continuous casting, these non-metallic inclusions are floated and separated in a tundish and the molten steel is poured into a mold as clean molten steel. However, it is difficult to float and separate very fine Al 2 O 3 inclusions of 50μ or less from steel, and no appropriate removal technology has been established at present. The present inventors conducted various tests for removing nonmetallic inclusions, and as a result, they found an effective filter for removing these fine Al 2 O 3 inclusions. i.e. consisting of lime clinker alone or 50wt%
This calcareous filter is made of a basic material consisting of the above lime clinker and the remainder is magnesia clinker or dolomite clinker, and has a large number of molten steel passage holes. The present inventors have obtained the knowledge through various experiments that calcareous refractories that come into contact with molten steel tend to bond with Al 2 O 3 in the steel and easily absorb it. The present invention makes active use of this phenomenon, and allows the molten steel to pass through a large number of molten steel passing holes to increase the chance of contact, thereby absorbing and removing the Al 2 O 3 inclusions in the molten steel. This is a removal filter. Al 2 O 3 inclusions in contact with lime undergo the reaction x・CaO + yAl 2 O 3 = xCaO・yAl 2 O 3 to form, for example, 3CaO・Al 2 O 3 , 12CaO・
Calcium aluminates such as 7Al 2 O 3 are easily generated and absorbed into the calcareous filter. One of the characteristics that a filter for removing nonmetallic inclusions must have is that it must not itself become a source of inclusions due to reaction with molten steel.
In the case of acidic refractories, Al in the steel reacts with SiO 2 , which is the main component of the refractory, to easily generate Al 2 O 3 according to the following formula. 4 Al + 3SiO 2 = 2Al 2 O 3 + 3 Si On the other hand, the basic materials used in the present invention, especially lime CaO, itself has a high melting point of 2500°C or higher, and its dissociated oxygen pressure and vapor pressure are low, making it stable even in vacuum. It is the most stable refractory material even against molten steel. Needless to say, the larger the proportion of CaO in the composition of the filter, the less likely it is that it will become a source of inclusions, and the better the reactivity of Al 2 O 3 will be.
If the CaO clinker ratio is less than 50wt%
There is a risk that the reactivity with Al 2 O 3 will decrease and the effectiveness for removing inclusions will decrease. The present inventors further investigated the material of the filter and found that by adding 1 to 20 wt% of CaCl 2 to lime or lime-magnesia (dolomite) material, Al 2 O 3 in molten steel could be more easily adsorbed. I found out. In other words, when using the filter of the present invention, depending on preheating or the temperature of molten steel,
Because it is heated above the melting point of CaCl 2 (772°C), CaCl 2 exists in a liquid phase. Therefore, it is considered that the absorbed Al 2 O 3 -based inclusions are easily moved into the inside of the filter and the absorption effect is increased.
The reason why the amount of CaCl 2 added is 20 wt% or less is because if it exceeds the amount, the amount of liquid phase becomes too large and the strength in hot conditions decreases, resulting in increased wear due to molten steel. Figure 1 shows Al 2 O 3 when lime and lime-CaCl 2 refractories are immersed in molten steel in a tundish.
It is a figure which shows the analysis example of the absorption of.

【表】 第1図にみるようにCaOの含有量が大きくかつ
CaCl2を添加しているものの方がAl2O3の吸収能
が大きくフイルターの材質として適することがわ
かる。 本発明による石灰質フイルターは通常の石灰質
耐火物の製造技術の範囲内で作られる。たとえば
石灰クリンカー、マグネシアクリンカーを粉砕、
粒度調整したものを非水系の油、レンジ等をバイ
ンダーとして混練し、適切な形状に鋳込み、振動
成形、加圧成形、あるいは抜き出しにより成形し
焼成する方法がとられる。あるいはCaCl2を含有
する場合は材料をCaCl2が溶融する772℃以上に
加熱しておきその温度域でフイルターの形状にホ
ツトプレスして成形することも可能である。 本発明による非金属介在物除去用フイルターを
用いる場所は例えば取鍋とタンデイツシユ間のロ
ングノズルの部品として、あるいはタンデイツシ
ユ内に堰の代りとして設置する、あるいはタンデ
イツシユと鋳型間のイマージヨンノズルの部品と
いう形で使用することが可能である。さらに
RH,DH等の精錬時の減圧容器内への設置も容易
である。フイルターの形状は設置される装置ある
いは容器に合せて適切な形が選ばれるが、溶鋼と
の接触面積を大きくするため溶鋼通過孔は直径が
小さくその数の多いものが望ましい。しかし溶鋼
の通過を妨げることなく非金属介在物を除去する
ため通過孔の大きさは5〜100mmφが適当であ
る。また溶鋼が通過する空隙の断面積はフイルタ
ー断面の20%以上が適当である。 以上述べたように本発明による石灰質フイルタ
ーは石灰あるいは石灰―CaCl2が溶鋼中のAl2O3
介在物と接触した場合容易にカルシウムアルミネ
ートを生成しフイルター内へ吸収しやすいという
特徴を利用したものであり、従来の非金属介在物
除去用フイルターが耐火物へAl2O3を単に吸着さ
せて除去することを目的としたものと異なりその
吸収能が非常に大きいことが特徴である。 以下に本発明による実施例を示す。 実施例1 (タンデイツシユへの適用例) 設置状況:第2図に示すように連鋳用タンデイ
ツシユ1内へフイルター2を2ケ所設置、 フイルターの材質:石灰石灰クリンカー95%+
CaCl25% フイルターの形状:鋼浴部分に対して20mmφの
孔を1m2当り100ケ、厚み100mm 転炉で溶製した鍋を取鍋からタンデイツシユに
注入し石灰質フイルター2ケ所を通過させて60t
の鋼材を製造した。取鍋内の溶鋼成分を表1に示
す。
[Table] As shown in Figure 1, the CaO content is large and
It can be seen that the material to which CaCl 2 is added has a greater ability to absorb Al 2 O 3 and is suitable as a filter material. The calcareous filter according to the invention is made within the scope of conventional calcareous refractory manufacturing techniques. For example, crushing lime clinker, magnesia clinker,
The particle size-adjusted product is kneaded with non-aqueous oil, microwave, etc. as a binder, cast into an appropriate shape, molded by vibration molding, pressure molding, or extrusion, and fired. Alternatively, if it contains CaCl 2 , it is possible to heat the material to 772° C. or higher, where CaCl 2 melts, and then hot-press and mold it into the shape of a filter in that temperature range. The filter for removing non-metallic inclusions according to the present invention can be used, for example, as a part of a long nozzle between a ladle and a tundish, or as a part of an immersion nozzle between a tundish and a mold. It is possible to use it in the form of moreover
It is also easy to install in a vacuum vessel during refining of RH, DH, etc. The shape of the filter is selected to suit the equipment or container in which it will be installed, but in order to increase the contact area with the molten steel, it is desirable that the molten steel passage holes have a small diameter and a large number. However, in order to remove nonmetallic inclusions without interfering with the passage of molten steel, the appropriate size of the passage hole is 5 to 100 mmφ. The cross-sectional area of the void through which molten steel passes is preferably at least 20% of the cross-section of the filter. As described above, in the calcareous filter according to the present invention, lime or lime-CaCl 2 is mixed with Al 2 O 3 in molten steel.
This method takes advantage of the fact that calcium aluminate is easily generated when it comes into contact with inclusions, and is easily absorbed into the filter. Conventional filters for removing non-metallic inclusions simply adsorb Al 2 O 3 to the refractory. It is characterized by its extremely high absorption capacity, unlike those whose purpose is to remove it. Examples according to the present invention are shown below. Example 1 (Example of application to tundish) Installation situation: As shown in Fig. 2, filters 2 are installed in two places in tundish 1 for continuous casting. Filter material: 95% lime clinker +
Shape of filter: 20mmφ holes in the steel bath part, 100 holes per 1m2 , thickness 100mm Pour 60t into a tundish from a ladle made in a converter and pass through two calcareous filters.
steel products were manufactured. Table 1 shows the composition of the molten steel in the ladle.

【表】 鋳造後の鋼のT.O=0.020% Al2O3介在物(30μ以上の検鏡介在物)=2.0
個/10cm2であり、比較例として通常のAl2O3質堰
を設けたタンデイツシユの場合T.O=0.025% Al2O3介在物(30μ以上の検鏡介在物)=8.5
個/10cm2であることから比べて本発明品のAl2O3
系介在物の除去能力がすぐれていることは顕著で
ある。 実施例2 (浸漬ノズルへの適用) 浸漬ノズルの先端に石灰質フイルターを設置し
タンデイツシユからの溶鋼を通過させた。 フイルターの材質:石灰クリンカー100% フイルターの形状:200mmφの円筒状フイルタ
ーに10mmφの孔を150ケあけた形状。 実施例1と同様の鋼60tを通過させて鋼材の介
在物を調査したところ、T・O=0.023 Al2O3介在物(30μ以上の検鏡介在物)=2.5
個/10cm2であり、フイルターを用いない場合(実
施例1の比較)よりも効果が明らかである。
[Table] TO of steel after casting = 0.020% Al 2 O 3 inclusions (speculum inclusions of 30μ or more) = 2.0
pieces/ 10cm2 , and as a comparative example, in the case of a tundish with a normal Al 2 O 3 weir, TO = 0.025% Al 2 O 3 inclusions (specular inclusions of 30μ or more) = 8.5
Al 2 O 3 of the invention product compared to
The ability to remove system inclusions is remarkable. Example 2 (Application to immersion nozzle) A calcareous filter was installed at the tip of the immersion nozzle to allow molten steel from the tundish to pass through. Filter material: 100% lime clinker Filter shape: 200mmφ cylindrical filter with 150 10mmφ holes. When 60 tons of steel similar to Example 1 was passed through to investigate inclusions in the steel material, T.O = 0.023 Al 2 O 3 inclusions (speculum inclusions of 30μ or more) = 2.5
/10cm 2 , and the effect is clearer than when no filter is used (comparison with Example 1).

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

第1図は石灰及び石灰―CaCl2質耐火物をタン
デイツシユ内の溶鋼中に浸漬したときのAl2O3
収の分析結果を示す図、第2図は実施例における
実施態様を示す図である。 1:タンデイツシユ、2:フイルター。
Figure 1 is a diagram showing the analysis results of Al 2 O 3 absorption when lime and lime-CaCl 2 refractories are immersed in molten steel in a tundish, and Figure 2 is a diagram showing embodiments in Examples. . 1: Tandem water, 2: Filter.

Claims (1)

【特許請求の範囲】 1 石灰クリンカー単独もしくは50wt%以上の
石灰クリンカーに残部がドロマイトクリンカー又
はマグネシアクリンカーからなり多数の溶鋼通過
孔を有することを特徴とする溶鋼の非金属介在物
除去用フイルター。 2 石灰クリンカー単独もしくは50wt%以上の
石灰クリンカーに残部がマグネシアクリンカー又
はドロマイトクリンカーとし、それに1〜20wt
%の塩化カルシウムを含有することを特徴とする
特許請求範囲第1項記載の溶鋼の非金属介在物除
去用フイルター。
[Scope of Claims] 1. A filter for removing non-metallic inclusions from molten steel, comprising lime clinker alone or 50 wt% or more of lime clinker with the remainder being dolomite clinker or magnesia clinker, and having a large number of molten steel passage holes. 2 Lime clinker alone or 50wt% or more of lime clinker with the balance being magnesia clinker or dolomite clinker, and 1 to 20wt%
% of calcium chloride, the filter for removing non-metallic inclusions from molten steel according to claim 1.
JP7604382A 1982-05-07 1982-05-07 Filter for removing non-metallic impurities of molten steel Granted JPS58193306A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7604382A JPS58193306A (en) 1982-05-07 1982-05-07 Filter for removing non-metallic impurities of molten steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7604382A JPS58193306A (en) 1982-05-07 1982-05-07 Filter for removing non-metallic impurities of molten steel

Publications (2)

Publication Number Publication Date
JPS58193306A JPS58193306A (en) 1983-11-11
JPS626606B2 true JPS626606B2 (en) 1987-02-12

Family

ID=13593765

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7604382A Granted JPS58193306A (en) 1982-05-07 1982-05-07 Filter for removing non-metallic impurities of molten steel

Country Status (1)

Country Link
JP (1) JPS58193306A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0628464U (en) * 1991-06-24 1994-04-15 三菱自動車工業株式会社 Flexible Tube
CN110257589A (en) * 2019-06-03 2019-09-20 邢台钢铁有限责任公司 Production Method for Reducing Calcium Aluminate Inclusions in Aluminum Killed Steel

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5486438A (en) * 1977-12-22 1979-07-10 Kobe Steel Ltd Production of clean steel
JPS6142672Y2 (en) * 1980-08-21 1986-12-03

Also Published As

Publication number Publication date
JPS58193306A (en) 1983-11-11

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