JPS5921697B2 - Continuous casting tandesh - Google Patents

Continuous casting tandesh

Info

Publication number
JPS5921697B2
JPS5921697B2 JP10654680A JP10654680A JPS5921697B2 JP S5921697 B2 JPS5921697 B2 JP S5921697B2 JP 10654680 A JP10654680 A JP 10654680A JP 10654680 A JP10654680 A JP 10654680A JP S5921697 B2 JPS5921697 B2 JP S5921697B2
Authority
JP
Japan
Prior art keywords
weir
upper weir
molten metal
push
continuous casting
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
JP10654680A
Other languages
Japanese (ja)
Other versions
JPS5731452A (en
Inventor
健 菅原
和雄 石山
三和人 野口
章生 石井
良昌 吉井
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 JP10654680A priority Critical patent/JPS5921697B2/en
Publication of JPS5731452A publication Critical patent/JPS5731452A/en
Publication of JPS5921697B2 publication Critical patent/JPS5921697B2/en
Expired 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
    • B22D11/118Refining the metal by circulating the metal under, over or around weirs

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Continuous Casting (AREA)

Description

【発明の詳細な説明】 本発明は溶融金属の連続鋳造において、上部?タンブツ
シュ内溶融金属表面より高くしだ上堰を設け、一方取鍋
ロングノズルから注入される溶融金属をタンプッシュ内
で上向流とするための上堰を上堰の内側に設置せしめて
溶融金属中の非金属介在物を浮上分離せしめる連続鋳造
タンプッシュに関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides continuous casting of molten metal. An upper weir is installed higher than the surface of the molten metal in the tumbler, and an upper weir is installed inside the upper weir to make the molten metal injected from the ladle long nozzle flow upward in the tumbler. This relates to a continuous casting tumble pusher that floats and separates non-metallic inclusions.

一般に取鍋からロングノズルを介してタンプッシュ内へ
溶融金属を注入する方法においては溶融金属の一部がタ
ンプッシュ底部に沿って流れ、鋳型内へ直ちに注入され
る場合がある。
Generally, in the method of injecting molten metal from a ladle into a tumbler through a long nozzle, a portion of the molten metal may flow along the bottom of the tumbler and be immediately injected into the mold.

このような鋳型内への直送流が生じるとタンプッシュ内
での溶融金属の滞溜時間が短かく溶融金属中の非金属介
在物(特にAl2O3系)の浮上分離が不十分であり、
鋳片や成品での介在物量が増加して鋳片品質を悪化させ
る。
When such a direct flow into the mold occurs, the residence time of the molten metal in the tamp push is short, and the floating separation of non-metallic inclusions (especially Al2O3 type) in the molten metal is insufficient.
The amount of inclusions in slabs and finished products increases, deteriorating the quality of slabs.

従来タンプッシュ内での非金属介在物の低減を目的とし
て種々の方法が知られている。
Conventionally, various methods are known for the purpose of reducing non-metallic inclusions within a tongue pusher.

第1図は従来の各種方法を示したものである。FIG. 1 shows various conventional methods.

第1図aに示す方法は2つの堰1,2により混合攪拌の
強化を計ったものである。
The method shown in FIG. 1a uses two weirs 1 and 2 to strengthen mixing and agitation.

この方法はAl2O3粒子同士を衝突させ凝集肥大化を
計り浮上分離を促進するものであるが、通常のタンプッ
シュ内の溶融金属の流量(1m3/min以下)では十
分な攪拌エネルギーは得られず微小なAl2O3粒子の
肥大化には限度があり、従って浮上分離の程度にも限界
がある。
In this method, Al2O3 particles collide with each other to cause agglomeration and enlargement to promote flotation and separation, but the flow rate of molten metal in a normal tump push (1 m3/min or less) does not provide sufficient stirring energy, resulting in very small particles. There is a limit to the enlargement of Al2O3 particles, and therefore there is also a limit to the degree of flotation separation.

第1図すに示す方法は取鍋ロングノズル直下に湯溜り堰
3を設けて注入流を上向きに整向せしめ、浮上分離を計
るものであるがロングノズルの外周に沿って溶融金属が
大気中に露出するため再酸化されて非金属介在物が生成
し再度金属浴中に巻込まれる欠点を有する。
In the method shown in Figure 1, a pool weir 3 is provided directly below the ladle long nozzle to orient the injected flow upward to achieve flotation and separation. Since it is exposed to water, it is reoxidized and non-metallic inclusions are generated, which have the disadvantage of being re-engulfed in the metal bath.

第1図Cに示す方法は一重堰付タンデッシュにより浮上
分離な促進するものである。
The method shown in FIG. 1C promotes flotation and separation using a tundish with a single weir.

この場合二つの堰4,4の間で溶融金属を上向きに揃え
、その後も浴面に沿った整流を形成して粒子の浮上分離
に好適な条件を与えるものである。
In this case, the molten metal is aligned upward between the two weirs 4, 4, and thereafter a rectified flow is formed along the bath surface to provide conditions suitable for floating and separating particles.

この方法の欠点は、前記a + bに示す方法に比較し
て攪拌エネルギーが大きくなることである。
A disadvantage of this method is that the stirring energy is greater than that of the method shown in a + b above.

従って粒子同士の衝突、凝集による肥大化にも限度があ
り、該粒子の浮上分離を促進せしめるには浮上分離に要
する時間を長くすること(即ちタンプッシュの大型化)
が必要となる。
Therefore, there is a limit to the size of particles due to collisions and agglomeration, and in order to promote flotation separation of particles, it is necessary to lengthen the time required for flotation separation (i.e., increase the size of the tongue push).
Is required.

以上述べた如く、従来の各種方法においては各種の堰を
タンプッシュに設けることにより、介在物の浮上分離率
を高めようとするものであり、それ以前の堰なしタンプ
ッシュに比較していずれも効果があることが知られては
いるが、これら各種の方法には上述の如く、単に攪拌強
化による粒子の凝集分離促進あるいは単に注入流を上向
流または浴面に沿って整流となし粒子が浮上分離し易い
条件を与えるにとyまっており、問題があった。
As mentioned above, in the various conventional methods, various types of weirs are installed in the tumble push to increase the flotation separation rate of inclusions, and compared to the previous tump push without a weir, all of them are Although these methods are known to be effective, as mentioned above, there are two methods: simply promoting agglomeration and separation of particles by strengthening agitation, or simply rectifying the injected flow in an upward direction or along the bath surface to prevent particles from flowing. There was a problem because it was too difficult to provide conditions that would facilitate flotation and separation.

本発明はこの欠点を除去するためタンブツシュ内溶融金
属表面上に上堰を設けてこの内側に介在物吸収能の高い
フラックスを滞溜させると共に、該上堰の内側で且つ取
鍋ロングノズルの直下付近に上堰を設け、該上堰によっ
て取鍋ロングノズルからの注入流を上向流として整向せ
しめ上堰内側に溜められたフラックスと溶融金属との接
触を強化してフラックスによる介在物の吸収除去を促進
せしめる方法である。
In order to eliminate this drawback, the present invention provides an upper weir on the surface of the molten metal in the tambutsu, accumulates a flux with high inclusion absorbing ability inside the weir, and deposits the flux inside the upper weir and directly below the ladle long nozzle. An upper weir is installed nearby, and the upper weir directs the flow injected from the ladle long nozzle into an upward flow, strengthens the contact between the flux accumulated inside the upper weir and the molten metal, and removes inclusions caused by the flux. This method promotes absorption and removal.

以下本発明の実施例シ示す図面によって詳細に説明する
Embodiments of the present invention will be described in detail below with reference to the drawings.

第2図a、bは母型タンプッシュにおける本発明の一例
を示す正面断面図および平面図である。
FIGS. 2a and 2b are a front sectional view and a plan view showing an example of the present invention in a mother tongue pusher.

取鍋5の下部に設げた取鍋ロングノズル6からの注入流
は上堰10によって上向流12に整向せしめられ、上堰
9の内側に溜められたフラックス11と接触しタンプッ
シュノズル8を通って鋳型内へ入る。
The injected flow from the ladle long nozzle 6 provided at the bottom of the ladle 5 is directed into an upward flow 12 by the upper weir 10, and comes into contact with the flux 11 accumulated inside the upper weir 9, and then flows into the tump push nozzle 8. pass through and enter the mold.

第3図a + bは箱型タンプッシュにおける本発明の
他の一例を示す正面断面図および平面図である。
FIGS. 3a and 3b are a front sectional view and a plan view showing another example of the present invention in a box-type tongue pusher.

この場合上堰9はタンプッシュを巾方向2分割するよう
にし、高さ方向は溶融金属流通孔9′を除いてタンプッ
シュ縦断面全面にわたって設置する。
In this case, the upper weir 9 is arranged to divide the tongue pusher into two parts in the width direction, and is installed over the entire vertical section of the tongue pusher in the height direction except for the molten metal flow hole 9'.

又上堰10は第3図すに示す如くタンプッシュ平面に於
て上堰9によって分割された部分の取鍋ロングノズル6
の浸漬側に設置する。
In addition, the upper weir 10 has a ladle long nozzle 6 in the portion divided by the upper weir 9 on the tongue push plane as shown in Figure 3.
Install it on the immersion side of the

溶融金属注入流は取鍋ロングノズル6から出た後、上堰
10によって上向流12に整向され、上堰9に設げた溶
融金属流通孔9′を通って分割された反対側に流入する
After the molten metal injected flow exits the ladle long nozzle 6, it is directed into an upward flow 12 by the upper weir 10, and flows into the opposite divided side through the molten metal flow hole 9' provided in the upper weir 9. do.

この間にフラックス11と接触し非金属介在物を捕捉す
る。
During this time, it comes into contact with the flux 11 and captures nonmetallic inclusions.

第4図a、l)はT型タンプッシュにおける本発明のさ
らに他の一例を示す正面断面図および平面図である。
FIGS. 4a and 4l) are a front sectional view and a plan view showing still another example of the present invention in a T-type tongue pusher.

このようにタンプッシュの形によって取鍋ロングノズル
を軸として対称形、非対称形に拘らずに上堰による上向
流と上堰の内側に溜めたフラックスとの接触反応を促進
させることが本発明の特徴である。
In this way, the present invention promotes the contact reaction between the upward flow from the upper weir and the flux accumulated inside the upper weir by the shape of the tongue push, regardless of whether it is symmetrical or asymmetrical with the ladle long nozzle as an axis. It is a characteristic of

本発明におげろ上堰の設置位置及び上堰の設置位置につ
いては適正な位置が存在する。
In the present invention, there are appropriate positions for installing the upper weir and the installation position of the upper weir.

即ち、第2.3.4図における上堰の内側面積S2 と
上堰の内側面積S1 との比S2/S1及び上堰内側
面積S1 の値を種々変化させて上堰内のフラックス中
のAl2O3濃度変化を調査し、Al2O3吸収能を評
価した。
That is, by varying the ratio S2/S1 of the inner area S2 of the upper weir to the inner area S1 of the upper weir and the inner area S1 of the upper weir in Fig. 2.3.4, the Al2O3 in the flux in the upper weir was changed. The concentration change was investigated and the Al2O3 absorption ability was evaluated.

尚フラックスは使用前成分Cab:51係、Sin:4
4係、Al2O3::3係、その他:残部のものを注入
溶鋼量に対して0.3に9/T使用した。
In addition, the flux is the component before use: Cab: 51, Sin: 4
Part 4, Al2O3: : Part 3, and the rest: 9/T were used at a ratio of 0.3 to the amount of molten steel injected.

第5図は以上のようにして測定したフラックス中Al2
O3濃度増加分(鋳造中と使用前の差)のデータを整理
して示した図である。
Figure 5 shows Al2 in the flux measured as above.
FIG. 3 is a diagram illustrating organized data on O3 concentration increase (difference between during casting and before use).

第5図より明らかなように81値がタンプッシュ内の溶
鋼表面積Sの175以下の場合には527S1比が大き
い方がフラックス中のAl2O3濃度が増加するが2.
0以上で飽和する傾向がある。
As is clear from Fig. 5, when the 81 value is less than 175 of the molten steel surface area S in the tank push, the Al2O3 concentration in the flux increases as the 527S1 ratio increases;
It tends to be saturated at 0 or more.

一方S1値がタンプッシュ内の溶鋼表面積の115を超
える場合にはAl2O3濃度の増加が小さい。
On the other hand, when the S1 value exceeds 115 of the surface area of the molten steel in the tamp push, the increase in the Al2O3 concentration is small.

以上の測定結果に基すきS1値をタンブツシュ内溶鋼表
面積の115以下とし、且つS2/S1比を2.0以上
とすることによって介在物(A1203)の吸収除去を
効果的に実施せしめるものである。
Based on the above measurement results, inclusions (A1203) can be effectively absorbed and removed by setting the S1 value to 115 or less of the surface area of molten steel in the tambutsu and setting the S2/S1 ratio to 2.0 or more. .

本発明タンプッシュを使用してブルーム鋳片(サイズ2
47X300・鋼種545C)を鋳造し、該鋳片を60
φの棒鋼として地疵倹査(JIS法)を実施した結果、
第1表に示す如く地疵成績の改善効果が認められた。
Using the tongue push of the present invention, bloom slabs (size 2)
47X300, steel type 545C), and the slab was
As a result of ground flaw inspection (JIS method) for φ steel bars,
As shown in Table 1, an improvement effect on ground defect results was observed.

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

第1図a + b s eはいずれも堰を設けた従来の
タンプッシュを示す正面断面図である。 第2〜第4図は本発明の実施例を示すもので、各各aは
正面断面図、bは平面図で、第2図は飛型タンプッシュ
に於ける例であり、第3図は箱型タンプッシュにおける
例であり、第4図はT型タンプッシュにおける例である
。 第5図は上堰、上堰の面積と介在物捕集の状況の関係を
示す図である。 1.2:堰、3:湯溜堰、4:堰、5:取鍋、6:取鍋
ロングノズル、7:タンプッシュ、8:タンプッシュノ
ズル、9・ト上堰、9′ :溶融金属流通孔、10:上
堰、11:フラックス、12:上向流。
FIGS. 1A, 1B, and 1E are front sectional views showing a conventional tongue pusher equipped with a weir. 2 to 4 show embodiments of the present invention, each a is a front sectional view, b is a plan view, FIG. 2 is an example of a flying tongue pusher, and FIG. 3 is a box This is an example of a T-type tongue push, and FIG. 4 is an example of a T-type tongue push. FIG. 5 is a diagram showing the relationship between the upper weir and the area of the upper weir and the state of inclusion collection. 1.2: Weir, 3: Weir, 4: Weir, 5: Ladle, 6: Ladle long nozzle, 7: Tongue push, 8: Tongue push nozzle, 9. Top weir, 9': Molten metal Flow hole, 10: Upper weir, 11: Flux, 12: Upward flow.

Claims (1)

【特許請求の範囲】[Claims] 1 連続鋳造タンプッシュにおいて上部をタンブツシュ
内溶融金属湯面より高くしだ上堰を設け、該上堰内側の
タンプッシュ底部に上堰を設置し、上堰の内側面積をS
l、上堰の内側面積をS2、タンブツシュ内溶鋼全表面
積をSとしたとき、S2/S1≦2.0とし且つSlく
15Sとしたことを特徴とする連続鋳造タンプッシュ
1. In a continuous casting tunpush, an upper weir is provided whose upper part is higher than the molten metal level in the tumbler, and an upper weir is installed at the bottom of the tungpush inside the upper weir, and the inner area of the upper weir is set to S.
1. A continuous casting tumble pusher characterized in that, where S2 is the inner area of the upper weir and S is the total surface area of molten steel in the tumbler, S2/S1≦2.0 and Sl is 15S.
JP10654680A 1980-08-02 1980-08-02 Continuous casting tandesh Expired JPS5921697B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10654680A JPS5921697B2 (en) 1980-08-02 1980-08-02 Continuous casting tandesh

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10654680A JPS5921697B2 (en) 1980-08-02 1980-08-02 Continuous casting tandesh

Publications (2)

Publication Number Publication Date
JPS5731452A JPS5731452A (en) 1982-02-19
JPS5921697B2 true JPS5921697B2 (en) 1984-05-22

Family

ID=14436351

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10654680A Expired JPS5921697B2 (en) 1980-08-02 1980-08-02 Continuous casting tandesh

Country Status (1)

Country Link
JP (1) JPS5921697B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6264795U (en) * 1985-10-07 1987-04-22

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4591135A (en) * 1984-08-15 1986-05-27 Inland Steel Company Fluid flow control structure for tundish
US4653733A (en) * 1984-10-03 1987-03-31 Inland Steel Company Tundish with fluid flow control structure
JPH0117410Y2 (en) * 1984-12-25 1989-05-19
US4828014A (en) * 1985-12-13 1989-05-09 Inland Steel Company Continuous casting tundish and assembly
US4754800A (en) * 1985-12-13 1988-07-05 Inland Steel Company Preventing undissolved alloying ingredient from entering continuous casting mold
US4711429A (en) * 1986-08-29 1987-12-08 Usx Corporation Tundish for mixing alloying elements with molten metal
CA2170530A1 (en) * 1993-08-28 1995-03-09 Michael Robert Clark Purifying molten metal
JP4714539B2 (en) * 2005-09-30 2011-06-29 新日本製鐵株式会社 Tundish for continuous casting
CN103240406B (en) * 2013-04-28 2015-05-27 首钢总公司 Continuous casting tundish and continuous casting tundish casting control method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6264795U (en) * 1985-10-07 1987-04-22

Also Published As

Publication number Publication date
JPS5731452A (en) 1982-02-19

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