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JPS6247621B2 - - Google Patents
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JPS6247621B2 - - Google Patents

Info

Publication number
JPS6247621B2
JPS6247621B2 JP58029399A JP2939983A JPS6247621B2 JP S6247621 B2 JPS6247621 B2 JP S6247621B2 JP 58029399 A JP58029399 A JP 58029399A JP 2939983 A JP2939983 A JP 2939983A JP S6247621 B2 JPS6247621 B2 JP S6247621B2
Authority
JP
Japan
Prior art keywords
molten steel
filter
tundish
inclusions
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.)
Expired
Application number
JP58029399A
Other languages
Japanese (ja)
Other versions
JPS59156556A (en
Inventor
Teruyoshi Hiraoka
Hiromu Fujii
Hiroshi Shimizu
Hiroshi Imawaka
Yoichi Yokoyama
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 JP2939983A priority Critical patent/JPS59156556A/en
Publication of JPS59156556A publication Critical patent/JPS59156556A/en
Publication of JPS6247621B2 publication Critical patent/JPS6247621B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/10Supplying or treating molten metal
    • B22D11/11Treating the molten metal
    • B22D11/116Refining the metal
    • B22D11/119Refining the metal by filtering

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Continuous Casting (AREA)
  • Casting Support Devices, Ladles, And Melt Control Thereby (AREA)

Description

【発明の詳細な説明】 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。 溶鋼中に存在し、凝固完了までに分離除去でき
ない非金属介在物は、鋼の加工性ならびに機械的
性質、成品での表面品質に悪影響を与える。 近年鋼材に要求される品質は次第に厳しくな
り、不純物の少いいわゆるスクリーンスチールが
求められている。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
を行う方法が用いられている。またH2、N2等の
脱ガスについてはRH式、DH式等の真空脱ガス装
置により処理がなされている。さらに脱酸生成物
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が浮上しにくく鋳片内に残
存することになり、これが成品品質を劣化させる
原因となる。通常、連続鋳造の場合はタンデイツ
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、100
μ以下の微細な非金属介在物や、Al2O3クラスタ
ーのような形態の介在物については、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、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と反応しやすく、
Al2O3を吸収しやすいという知見を得た。その実
験結線の一例を第1図に示す。この図は、連鋳タ
ンデイツシユのセキに使われた石灰質耐火物
(CaO93%、残部MgO)の耐火物表面からの
Al2O3含有量分布であり、Al2O3が耐火物表面か
ら20mm程度まで浸透しているのがわかる。また、
この試験結果は、4ch(400t)鋳造した後の結果
であるが、石灰質耐火物は、ほとんど溶損されて
おらず、溶鋼中への反応生成物(a(CaO)・b
(Al2O3))の混入が無いことを示しており、反応
生成物自身が介在物起源にならないことがわか
る。このことかな、石灰質耐火物を溶鋼と接触さ
せることにより、溶鋼中のAl2O3が分離除去でき
るわけであり、本発明はこの現象を積極的に利用
することが第1の要点である。 次に第2の要点は、タンデイツシユの内部に、
第2図、第3図A,Bに示すごとく、石灰質耐火
物製の円筒1を積重ねることである。 すなわち、積重ねる位置は第2図に示す如く、
タンデイツシユ2への注入ロングノイズ3と鋳型
への鋳込みノズル4との間の任意の位置において
1ケ所以上である。積重ねる方向は円筒の中止軸
の方向をタンデイツシユの溶鋼流動方向に一致さ
せて設置するものであり、これにより円筒と溶鋼
の接触チヤンスを増すと共に、このフイルターを
通過後、溶鋼の流れを整流にすることにより、タ
ンデイツシユの溶鋼湯面にあるスラグや保温剤の
巻込みを防止するものである。尚、図中5は浮上
防止用の押え板を示している。 次に本発明フイルターと関連先行技術との差異
について述べる。 先づ最初に多数の貫通孔を有するセキとの差異
について述べれば、この技術では、溶鋼が接触す
るのは貫通孔の内面のみで溶鋼の接触面積が少な
い。これに対して本発明のフイルターは円筒状耐
火物で、且つこれを多段積重ねたものであるの
で、円筒の内外両面に溶鋼が接触して接触面積が
著しく増加する結果、介在物の吸着効果は極めて
大きい。 次に特開昭56−1252号により耐火物製棚よりな
るフイルターが提案されている。この棚フイルタ
ーと本発明フイルターとの相違点は、第1に、棚
フイルターの場合には、1枚1枚タンデイツシユ
に固定する必要があり、タンデイツシユの築造が
著しく困難であるのに対して、本発明フイルター
では円筒をタンデイツシユ内で積重ね、最終的に
これを1枚の押え板で押えればよくフイルターの
設置が極めて簡単であることである。次にその第
2点の棚フイルターの場合には溶鋼との接触が平
面接触であるのに対して本発明フイルターでは多
数の円筒による曲面接触で、本発明フイルターの
方が溶鋼との接触面積が大きく、それだけ介在物
の吸着能力が大きいことである。 円筒状にして積み重ねるもう一つの理由は、タ
ンデイツシユの予熱時に十分に予熱ガスが通り、
溶鋼注入時にそのフイルター部で溶鋼が固まらな
いような温度にまでセキを加熱することを容易な
らしめるためである。すなわち、特開昭56−
47509のごとく粒状耐火物にてフイルターを構成
した場合、粒状耐火物の積み重なり状況の微妙な
異いから、ガス流の通過場所に不均一が生じ、そ
の結果として、フイルターの一部が詰まり、溶鋼
が流れにくくなる結果、所定の鋳造速度が得られ
なくなる場合が生じた。ところが、本発明のごと
く石灰質耐火物を円筒状にすることによりフイル
ター全体が均一に予熱され、溶鋼づまりのような
トラブルが生じなくなるわけである。ただし、フ
イルターの横断面での空間の面積率が、少なくな
つたり、円筒の長さが長くなると溶鋼との接触率
は増大するものの、フイルター部での溶鋼の圧損
が大きくなり、タンデイツシユの形状などが複雑
になるため、タンデイツシユの形状、単位時間当
りの鋳造量などを考慮して適正なものにする必要
がある。 以下に本発明による具体的効果を実施例並びに
比較例をもつて説明する。 実施例 転炉出鋼後、RH真空脱ガス装置内で微調整し
た第1表に示すような溶鋼を、肉厚40mm、外径80
mm、長さ100mmの石灰系円筒状耐火物25個をTDの
底から3個、4個、5個、6個、7個と5段に積
んで上方から、これらの耐火物が浮かないように
ハイアルミナ系耐火物の押え板により押えて構成
されたフイルターを設けたタンデイツシユに受
け、鋳型内に浸漬ノズルにより、第1表に示すよ
うな条件にて鋳造した。 その結果、T.O=25ppm、Al2O3系介在物は、
顕微鏡観察で53個/25mm2の極めて清浄な鋼が得ら
れ、成品ブリキでの磁探欠陥発生率が2ケ/1000
m2と非常に良好な成績であつた。 比較例 実施例の比較試験としてほぼ同成分(第1表に
示す)の溶鋼を実施例と同じ工程で溶製し、通常
のフイルターのないタンデイツシユに受け、鋳型
内に浸漬ノズルにより、実施例と同一の鋳造条件
にて鋳造した。 その結果、T.O=38ppm、Al2O3系介在物、124
個/25mm2、成品ブリキでの磁探欠陥発生率が6
ケ/1000m2と介在物フイルター設置に比較して鋳
片での清浄性ならびに成品品質は劣つていた。 以上、実施例並びに比較例からも明らかなよう
に本発明による非金属介在物除去フイルターは極
めて有益なものであるといえる。 【表】
[Detailed description of the invention] 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. Nonmetallic inclusions that are present in molten steel and cannot be separated and removed before solidification is completed have an adverse effect on the workability and mechanical properties of the steel, as well as the surface quality of the finished product. In recent years, the quality required for steel materials has become increasingly strict, and so-called screen steel with fewer impurities is now in demand. A conventional method for removing impurities is to add a refining agent (flux) such as CaO, CaF 2 or Na 2 CO 3 to hot metal or molten steel to perform desulfurization and dephosphorization treatment. Furthermore, degassing of H 2 , N 2 , etc. is carried out using a vacuum degassing device such as an RH type or a DH type. Furthermore, removal of deoxidation products, that is, nonmetallic inclusions, is also an important point in cleaning molten steel. Particularly in the case of Al-deoxidized steel, the deoxidized product Al 2 O 3 is difficult to float and remains in the slab, which causes deterioration of product quality. 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. But 100
Currently, it is difficult to float and separate microscopic nonmetallic inclusions smaller than µ or inclusions in the form of Al 2 O 3 clusters from steel, and no appropriate removal technology has been established. . The present inventors have found through various experiments that calcareous refractories that come into contact with molten steel tend to react with Al 2 O 3 in the steel.
We obtained the knowledge that Al 2 O 3 is easily absorbed. An example of the experimental connection is shown in FIG. This figure shows the surface of a calcareous refractory (93% CaO, balance MgO) used in a continuous casting tandem.
This is the Al 2 O 3 content distribution, and it can be seen that Al 2 O 3 has penetrated to about 20 mm from the refractory surface. Also,
This test result was obtained after casting 4ch (400t), but the calcareous refractory was hardly eroded and the reaction products (a(CaO), b
This shows that there is no contamination of (Al 2 O 3 )), indicating that the reaction product itself is not the source of inclusions. This means that Al 2 O 3 in the molten steel can be separated and removed by bringing the calcareous refractory into contact with the molten steel, and the first point of the present invention is to actively utilize this phenomenon. Next, the second point is that inside the tundish,
As shown in FIGS. 2 and 3A and 3B, cylinders 1 made of calcareous refractories are stacked one on top of the other. In other words, the stacking positions are as shown in Figure 2.
One or more arbitrary positions between the injection long noise 3 into the tundish 2 and the casting nozzle 4 into the mold. The direction in which the cylinders are stacked is such that the axis of the cylinders matches the direction of the flow of molten steel in the tundish.This increases the chance of contact between the cylinders and molten steel, and also straightens the flow of molten steel after passing through this filter. This prevents the slag and heat insulating agent on the surface of the molten steel in the tundish from becoming entangled. In addition, numeral 5 in the figure indicates a holding plate for preventing floating. Next, the differences between the filter of the present invention and related prior art will be described. First of all, let's talk about the difference between this technique and the conventional technique, which has a large number of through holes.With this technology, the molten steel comes into contact only with the inner surface of the through holes, and the contact area of the molten steel is small. On the other hand, since the filter of the present invention is a cylindrical refractory material and is made of multi-layered refractories, the molten steel contacts both the inner and outer surfaces of the cylinder, significantly increasing the contact area, and as a result, the effect of adsorbing inclusions is reduced. Extremely large. Next, JP-A-56-1252 proposes a filter made of a refractory shelf. The difference between this shelf filter and the filter of the present invention is that, first, in the case of a shelf filter, it is necessary to fix each filter to a tundish tray, making it extremely difficult to construct a tundish tray. The filter of the invention is extremely easy to install by stacking the cylinders in a tundish and finally pressing them down with a single holding plate. Next, in the case of the second shelf filter, the contact with the molten steel is a plane contact, whereas in the filter of the present invention, the contact is a curved surface with a large number of cylinders, and the contact area with the molten steel is larger in the filter of the present invention. The larger the size, the greater the ability to adsorb inclusions. Another reason for stacking them in a cylindrical shape is to allow sufficient preheating gas to pass through when preheating the tundish.
This is to make it easier to heat the steel to a temperature that will prevent the molten steel from solidifying in the filter section when pouring molten steel. In other words, JP-A-56-
When a filter is made of granular refractories like 47509, subtle differences in the way the granular refractories are piled up create unevenness in the passage of the gas flow, resulting in part of the filter becoming clogged and causing the molten steel to become clogged. As a result, it became difficult to obtain the desired casting speed. However, by forming the calcareous refractory into a cylindrical shape as in the present invention, the entire filter is preheated uniformly, and troubles such as clogging of molten steel do not occur. However, if the area ratio of the space in the cross section of the filter decreases or the length of the cylinder increases, the contact rate with the molten steel will increase, but the pressure loss of the molten steel at the filter will increase, and the shape of the tundish will change. Since the process becomes complicated, it is necessary to consider the shape of the tundish, the amount of casting per unit time, etc. to make it appropriate. The specific effects of the present invention will be explained below using Examples and Comparative Examples. Example After tapping the steel from the converter, the molten steel as shown in Table 1, which was finely adjusted in the RH vacuum degassing equipment, was heated to a wall thickness of 40 mm and an outer diameter of 80 mm.
25 pieces of lime-based cylindrical refractories with a length of 100 mm are stacked in 5 tiers of 3, 4, 5, 6, and 7 from the bottom of the TD, and stacked from above to prevent these refractories from floating. The sample was placed in a tundish equipped with a filter held down by a high alumina refractory holding plate, and cast into a mold using an immersion nozzle under the conditions shown in Table 1. As a result, TO=25ppm, Al 2 O 3 inclusions were
Extremely clean steel with 53 pieces/ 25mm2 was obtained by microscopic observation, and the magnetic detection defect occurrence rate in finished tinplate was 2 pieces/1000.
m2 , which was a very good result. Comparative Example As a comparative test with the example, molten steel with almost the same composition (shown in Table 1) was melted in the same process as the example, passed through a normal tundish without a filter, and placed into the mold with an immersion nozzle to form a molten steel with the same composition as the example. Casting was performed under the same casting conditions. As a result, TO=38ppm, Al2O3 - based inclusions, 124
pieces/25mm 2 , magnetic detection defect occurrence rate in finished tinplate is 6
KE/1000m 2 The cleanliness and product quality of the cast slab were inferior compared to the case where an inclusion filter was installed. As is clear from the Examples and Comparative Examples above, it can be said that the filter for removing non-metallic inclusions according to the present invention is extremely useful. 【table】

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

第1図は鋳造後のタンデイツシユの石灰系耐火
物の表面からのAl2O3含有量変化の図であり、第
2図及び第3図A,Bは本発明による非金属介在
物除去フイルターをタンデイツシユに設置した場
合の図である。 1……石灰系の筒状耐火物、5……浮上防止押
え板。
Fig. 1 is a diagram showing the change in Al 2 O 3 content from the surface of the lime-based refractory of the tundish after casting, and Fig. 2 and Fig. 3 A and B show the nonmetallic inclusion removal filter according to the present invention. It is a diagram when it is installed in a tandem tray. 1... Lime-based cylindrical refractory material, 5... Anti-surfacing holding plate.

Claims (1)

【特許請求の範囲】[Claims] 1 連続鋳造用タンデイツシユの取鍋からの注入
位置とタンデイツシユから連続鋳造用鋳型への注
入位置との間に、石灰系の筒状耐火物の重層物を
タンデイツシユ内溶鋼の溶鋼流動方向に対して、
円筒の軸方向を平行にして、1箇所以上設置し、
微小Al2O3介在物を吸着させるようにしたことを
特徴とする、溶鋼の非金属介在物除去フイルタ
ー。
1. Between the injection position from the ladle of the continuous casting tundish and the injection position from the tundish into the continuous casting mold, a multi-layered lime-based cylindrical refractory is placed in the direction of flow of molten steel in the tundish.
Install it in one or more locations with the axial direction of the cylinder parallel,
A filter for removing non-metallic inclusions from molten steel, characterized in that it adsorbs minute Al 2 O 3 inclusions.
JP2939983A 1983-02-25 1983-02-25 Filter for removing nonmetallic inclusion in molten steel Granted JPS59156556A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2939983A JPS59156556A (en) 1983-02-25 1983-02-25 Filter for removing nonmetallic inclusion in molten steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2939983A JPS59156556A (en) 1983-02-25 1983-02-25 Filter for removing nonmetallic inclusion in molten steel

Publications (2)

Publication Number Publication Date
JPS59156556A JPS59156556A (en) 1984-09-05
JPS6247621B2 true JPS6247621B2 (en) 1987-10-08

Family

ID=12275059

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2939983A Granted JPS59156556A (en) 1983-02-25 1983-02-25 Filter for removing nonmetallic inclusion in molten steel

Country Status (1)

Country Link
JP (1) JPS59156556A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61117360U (en) * 1984-12-28 1986-07-24

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS561252A (en) * 1979-06-14 1981-01-08 Sumitomo Electric Ind Ltd Tundish for continuous casting

Also Published As

Publication number Publication date
JPS59156556A (en) 1984-09-05

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