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JPS6358069B2 - - Google Patents
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JPS6358069B2 - - Google Patents

Info

Publication number
JPS6358069B2
JPS6358069B2 JP25145583A JP25145583A JPS6358069B2 JP S6358069 B2 JPS6358069 B2 JP S6358069B2 JP 25145583 A JP25145583 A JP 25145583A JP 25145583 A JP25145583 A JP 25145583A JP S6358069 B2 JPS6358069 B2 JP S6358069B2
Authority
JP
Japan
Prior art keywords
electromagnetic stirring
value
current value
molten steel
current
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
JP25145583A
Other languages
Japanese (ja)
Other versions
JPS60145258A (en
Inventor
Isao Suzuki
Miwato Noguchi
Juji Senda
Hitoshi Demachi
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 JP25145583A priority Critical patent/JPS60145258A/en
Publication of JPS60145258A publication Critical patent/JPS60145258A/en
Publication of JPS6358069B2 publication Critical patent/JPS6358069B2/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
    • B22D11/114Treating the molten metal by using agitating or vibrating means
    • B22D11/115Treating the molten metal by using agitating or vibrating means by using magnetic fields

Landscapes

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

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は電磁撹拌装置を有する連続鋳造設備に
於いて、電磁撹拌によつて生じる負偏析が鋳造条
件の変化にかかわらず常に目標値に保持されるよ
う電流値を制御する方法に係るものである。
Detailed Description of the Invention (Field of Industrial Application) The present invention provides continuous casting equipment equipped with an electromagnetic stirring device in which negative segregation caused by electromagnetic stirring is always maintained at a target value regardless of changes in casting conditions. This relates to a method of controlling the current value so that the

(従来技術) 一般に、電磁撹拌装置を有する連続鋳造設備で
は、等軸晶率の増加、中心偏析の低減を目的に、
凝固中の鋳片内溶鋼に対して電磁撹拌を行なつて
いる。その場合撹拌電流の増加に伴なつて凝固前
面の溶鋼推力は増加し、結果的に等軸晶率の増
加、中心偏析の偏析度軽減等の効果が得られる。
(Prior art) Generally, in continuous casting equipment equipped with an electromagnetic stirring device, for the purpose of increasing equiaxed crystallinity and reducing center segregation,
Electromagnetic stirring is applied to the molten steel in the slab during solidification. In this case, as the stirring current increases, the molten steel thrust at the solidification front increases, resulting in effects such as an increase in equiaxed crystallinity and a reduction in the degree of segregation at the center.

しかしその反面、凝固中の溶鋼を撹拌する事に
より凝固前面が溶鋼による洗浄効果を受け凝固前
面の液相濃度が低下する。液相濃度が低下すると
その溶鋼の平衡分配係数に応じて凝固前面の固相
側の溶質濃度が低下し、結果的に電磁撹拌によつ
て溶鋼撹拌を行なつた部分の鋳片に、一般的にホ
ワイトバンドと呼ばれる負偏析帯が生じる。ホワ
イトバンドすなわち負偏析帯の偏析度合が大きい
と鋼材の焼入性及び機械的性質に支障をきたす場
合がある。
However, on the other hand, by stirring the solidifying molten steel, the solidifying front receives the cleaning effect of the molten steel, and the liquid phase concentration at the solidifying front decreases. When the liquid phase concentration decreases, the solute concentration on the solid phase side at the solidification front decreases according to the equilibrium distribution coefficient of the molten steel, and as a result, the molten steel is stirred by electromagnetic stirring. A negative segregation band called the white band occurs. If the degree of segregation of the white band, that is, the negative segregation zone is large, it may impede the hardenability and mechanical properties of the steel material.

従来この問題解決のため、いくつかの提案がな
されている。例えば、特公昭53−25533号に開示
された技術は、最適な電磁撹拌電流値を求める
際、まず撹拌位置における凝固殻厚みを推定し、
これを基に撹拌装置の電源周波数を求め、この値
から電流値を求めるものであるが、この方法は精
度に劣る難点を有する。又、他の先行技術として
は特開昭58−112643号に示される技術がある。該
技術は電磁撹拌電流値を得る際、冷却水の流量、
鋳型入出側水温、鋳片の引抜速度、鋳片溶融部の
所定撹拌速度を基にして求めるものであるが、本
方法も前記同様精度に疑問がある。
Several proposals have been made to solve this problem. For example, in the technology disclosed in Japanese Patent Publication No. 53-25533, when determining the optimum electromagnetic stirring current value, the thickness of the solidified shell at the stirring position is first estimated,
Based on this, the power supply frequency of the stirring device is determined, and the current value is determined from this value, but this method has the drawback of poor accuracy. Further, as another prior art, there is a technique shown in Japanese Patent Application Laid-Open No. 112643/1983. In this technology, when obtaining the electromagnetic stirring current value, the flow rate of cooling water,
Although it is determined based on the water temperature at the entrance and exit side of the mold, the drawing speed of the slab, and the predetermined stirring speed of the molten zone of the slab, this method is also questionable in its accuracy as described above.

(発明の目的) 本発明は、前記状況に鑑みなされたもので、シ
エル厚に応じて変化する最適電流値を精度良く求
めて、該最適電流値に制御することが可能な方法
を得ることを目的とする。
(Object of the Invention) The present invention has been made in view of the above-mentioned situation, and aims to provide a method capable of accurately determining the optimum current value that changes depending on the shell thickness and controlling the current value to the optimum current value. purpose.

(発明の構成と作用) 本発明は電磁撹拌位置での凝固シエル厚と目標
ホワイトバンドの設定値とからモデル式を用いて
最適電磁撹拌電流値を求めて、その値を基に撹拌
装置の電流制御を行なうものである。
(Structure and operation of the invention) The present invention uses a model formula to determine the optimum electromagnetic stirring current value from the solidified shell thickness at the electromagnetic stirring position and the set value of the target white band, and based on that value, the current value of the stirring device is It is for controlling.

即ち、電磁撹拌を行なう連続鋳造において、電
磁撹拌装置前面の凝固シエル厚をD、実効分配係
数をKE、平衡分配係数をKp、必要電流値をAと
し、係数gを与えて、 で算出した電流値Aの±15%の範囲内に電磁撹拌
装置の電流を制御することを特徴とする連続鋳造
における電磁撹拌電流の制御方法である。
That is, in continuous casting using electromagnetic stirring, the solidified shell thickness in front of the electromagnetic stirring device is D, the effective distribution coefficient is K E , the equilibrium distribution coefficient is K P , the required current value is A, and the coefficient g is given. This is a method for controlling an electromagnetic stirring current in continuous casting, characterized by controlling the current of an electromagnetic stirring device within a range of ±15% of the current value A calculated in .

以下、さらに詳細に説明する。 This will be explained in more detail below.

本発明者等は、従来からそれ自体は知られてい
る物質流動下での凝固式を、溶鋼の連続鋳造操業
要素と対応させた結果、凝固シエル厚Dで整理す
ると良好な結果が得られることを知得した。そこ
で溶鋼の流速Uが電磁撹拌推力Hの平方に比例す
ると仮定し、凝固前面における洗浄深さをSh、
凝固速度をfとすると、ホワイトバンド生成の経
験式として下記(1)式が導き出される。
The present inventors have made the solidification equation under material flow, which has been known in the past, correspond to the operational elements of continuous casting of molten steel, and have found that good results can be obtained by organizing the solidification shell thickness D. learned. Therefore, assuming that the flow velocity U of molten steel is proportional to the square of the electromagnetic stirring thrust H, the cleaning depth at the solidification front is Sh,
When the solidification rate is f, the following formula (1) can be derived as an empirical formula for white band generation.

一方実効分配係数をKE、平衡分配係数をKp
して物質保存則より下記(2)式が成り立つ。
On the other hand, the following equation (2) holds true according to the law of conservation of matter, where the effective partition coefficient is K E and the equilibrium partition coefficient is K p .

KE=1−(1−Kp)・Sh ……(2) ここで実効分配係数KEと平衡分配係数Kpにつ
いて説明する。第1図は溶鋼撹拌による凝固前面
の溶質濃度変化の状況を表わし、第1図aは電磁
撹拌なし、第1図bは電磁撹拌ありの場合を夫々
示しており、図中の各記号の意味は次のとおりで
ある。
K E =1-(1-K p )·Sh (2) Here, the effective partition coefficient K E and the equilibrium partition coefficient K p will be explained. Figure 1 shows the change in solute concentration at the front of solidification due to stirring of molten steel. Figure 1 a shows the case without electromagnetic stirring, and Figure 1 b shows the case with electromagnetic stirring. The meaning of each symbol in the figure. is as follows.

Cs:撹拌のない場合の固相濃度 CL: 〃 液相濃度 Cs′:撹拌のある場合の固相濃度 CL′: 〃 液相濃度 Cp:平均濃度 Kp:平衡分配係数 KE:実効分配係数 実効分配係数KEは固相濃度Cs(又はCs′)と平
均濃度Cpとの比Cs/Cpであり、平衡分配係数Kp
は固相濃度Cs(又はCs′)と液相濃度CL(又はCL′)
との比Cs/CL)で表わす。又、電磁撹拌推力H
は電流Aと2乗に比例し、又電流が一定ならば電
磁撹拌用コアー間の推力Hはコアー間の位置で決
まる。すなわち推力Hはシエル厚Dから求まり下
記(3)式で得られる。
C s : Solid phase concentration without stirring C L : 〃 Liquid phase concentration C s ′: Solid phase concentration with stirring C L ′: 〃 Liquid phase concentration C p : Average concentration K p : Equilibrium partition coefficient K E : Effective partition coefficient The effective partition coefficient K E is the ratio C s /C p between the solid phase concentration C s (or C s ′) and the average concentration C p , and the equilibrium partition coefficient K p
are the solid phase concentration C s (or C s ′) and the liquid phase concentration C L (or C L ′)
It is expressed as the ratio C s /C L ). In addition, electromagnetic stirring thrust H
is proportional to the square of the current A, and if the current is constant, the thrust H between the electromagnetic stirring cores is determined by the position between the cores. That is, the thrust force H is determined from the shell thickness D and is obtained by the following equation (3).

H=A2・g ……(3) ここでgはシエル厚Dと電磁撹拌装置の形状、
即ちポールピツチ、コア間距離によつて決まる係
数で、通常1.0×10-8〜0.1の間の値をとり、推力
Hの分布を規定する。ポールピツチが大きくなる
に従つて大きい値とし、逆にポールピツチが小に
なるに従つて小さい値をとる。又コア間距離が大
になるに従つて小さい値とし、逆にコア間距離が
小になるに従つて大きい値とする。一例としてポ
ールピツチ722mm,コア間距離447mm,シエル厚D
が30mm〜175mmの場合で、2.1×10-5〜1.2×10-6
間が適当である。
H=A 2・g...(3) Here, g is the shell thickness D and the shape of the electromagnetic stirring device,
That is, it is a coefficient determined by the pole pitch and the distance between cores, usually takes a value between 1.0×10 -8 and 0.1, and defines the distribution of thrust H. As the pole pitch increases, the value increases, and conversely, as the pole pitch decreases, the value decreases. Further, as the distance between the cores becomes larger, the value becomes smaller, and conversely, as the distance between the cores becomes smaller, the value becomes larger. As an example, pole pitch is 722mm, distance between cores is 447mm, and shell thickness is D.
is between 30 mm and 175 mm, and a range between 2.1×10 −5 and 1.2×10 −6 is appropriate.

ホワイトバンドは、実効分配係数KEと一対一
の対応があるので、目標ホワイトバンドが与えら
れた場合の必要電流値Aは前記(1)〜(3)式より下記
(4)式のように求まる。
Since the white band has a one-to-one correspondence with the effective distribution coefficient K E , the required current value A when the target white band is given is as follows from equations (1) to (3) above.
It can be found as in equation (4).

上記により求めた電流値Aは最適値であるが、
一定の範囲であれば効果を損なうことはなく、そ
の範囲は±15%である。
The current value A obtained above is the optimal value, but
The effect will not be impaired within a certain range, and the range is ±15%.

前記(4)式においてシエル厚Dは第2図に示すよ
うに求められる。即ち、まずプロセス情報として
タンデイツシユ内溶鋼の過熱温度、モールド内で
の抜熱量、及び2次冷却水量を収集する。次に2
次冷却水量を熱伝達率に評価し直し、シエル厚の
推定計算を行ない、電磁撹拌位置でのシエル厚を
求める事ができる。シエル厚D以外の項は既知で
あり、即ちKEは目標とするホワイトバンドによ
り、Kpは鋼種により決まるので目標とする電磁
撹拌電流Aは、前記(4)式より求める事ができる。
In the above equation (4), the shell thickness D is determined as shown in FIG. That is, first, the superheating temperature of the molten steel in the tundish, the amount of heat removed in the mold, and the amount of secondary cooling water are collected as process information. Next 2
Next, the amount of cooling water is reevaluated to the heat transfer coefficient, and the estimated shell thickness is calculated to determine the shell thickness at the electromagnetic stirring position. Since the terms other than the shell thickness D are known, that is, K E is determined by the target white band, and K P is determined by the steel type, the target electromagnetic stirring current A can be determined from the above equation (4).

なお、第2図に於て、1は溶鋼鍋、2はタンデ
ツシユ、3はモールド、4はスプレーゾーン、5
は電磁撹拌装置である。
In Fig. 2, 1 is the molten steel ladle, 2 is the tundish, 3 is the mold, 4 is the spray zone, and 5 is the molten steel ladle.
is an electromagnetic stirring device.

このように本発明方法によれば、操業条件が変
化しても常に目標のホワイトバンドとなるよう
に、言い換えれば常に溶鋼前面の推力が一定とな
るように電磁撹拌電流をコントロールする事が可
能となる。
In this way, according to the method of the present invention, it is possible to control the electromagnetic stirring current so that the target white band is always achieved even if the operating conditions change, or in other words, the thrust at the front of the molten steel is always constant. Become.

(実施例) 第2図に示す連続鋳造設備において、タンテツ
シユ内溶鋼の過熱温度26℃、モールド内抜熱量
18800Kcal/min、2次冷却水量410/minのデ
ータから計算機により電磁撹拌装置前面のシエル
厚D=71mmを求めた。gは本実施例の電磁撹拌装
置の形状から0.8×10-5とした。また、実効分配
係数(即ちホワイトバンド目標値)はKE=0.93と
し、平衡分配係数はKp=0.34と置くと(4)式から電
流値Aは、A=450アンペアを得た。この値をも
とに電磁撹拌装置の電流制御を行なつた。尚、前
記シエル厚Dは一定時間毎(48秒)に計算し、そ
の都度最適電流値の計算を行ないその値を基に電
流制御を行なつた結果、従来法に比較し等軸晶率
が10%向上し、これに比例して中心偏析が低減し
た。
(Example) In the continuous casting equipment shown in Fig. 2, the superheating temperature of the molten steel in the tantestine was 26℃, and the amount of heat extracted in the mold was
A shell thickness D = 71 mm in front of the electromagnetic stirring device was determined by a computer from data of 18,800 Kcal/min and secondary cooling water flow rate of 410/min. g was set to 0.8×10 −5 based on the shape of the electromagnetic stirring device of this example. Further, when the effective distribution coefficient (ie, white band target value) is set as K E =0.93 and the equilibrium distribution coefficient is set as K P =0.34, the current value A is obtained from equation (4) as A = 450 amperes. Based on this value, the current of the electromagnetic stirring device was controlled. The shell thickness D is calculated at regular intervals (48 seconds), the optimum current value is calculated each time, and the current is controlled based on that value. As a result, the equiaxed crystallinity is lower than that of the conventional method. This was improved by 10%, and center segregation was reduced proportionally.

(発明の効果) 以上説明した通り、本発明を適用することによ
り、電磁撹拌装置の電流値を目標とする値に制御
することができ品質改善に効果がある。
(Effects of the Invention) As explained above, by applying the present invention, the current value of the electromagnetic stirring device can be controlled to a target value, which is effective in improving quality.

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

第1図は溶鋼撹拌による凝固前面の溶質濃度変
化の状況説明図で、aは電磁撹拌なし、bは電磁
撹拌ありを夫々示す。第2図は本発明の制御方法
の説明図である。 1:溶鋼鍋、2:タンデツシユ、3:モール
ド、4:スプレーゾーン、5:電磁撹拌装置。
FIG. 1 is an explanatory diagram of the change in solute concentration at the front of solidification due to stirring of molten steel, where a shows the case without electromagnetic stirring and b shows the case with electromagnetic stirring. FIG. 2 is an explanatory diagram of the control method of the present invention. 1: Molten steel pot, 2: Tandeshi, 3: Mold, 4: Spray zone, 5: Electromagnetic stirring device.

Claims (1)

【特許請求の範囲】 1 電磁撹拌を行なう連続鋳造において、電磁撹
拌装置前面の凝固シエル厚をD、実効分配係数を
KE、平衡分配係数をKp、必要電流値をAとし、
係数gを与えて、 で算出した電流値Aの±15%の範囲内に電磁撹拌
装置の電流を制御することを特徴とする連続鋳造
における電磁撹拌電流の制御方法。
[Claims] 1. In continuous casting using electromagnetic stirring, the thickness of the solidified shell in front of the electromagnetic stirring device is D, and the effective distribution coefficient is
K E , the equilibrium distribution coefficient is K p , the required current value is A,
Given the coefficient g, A method for controlling an electromagnetic stirring current in continuous casting, characterized by controlling the current of an electromagnetic stirring device within a range of ±15% of the current value A calculated in .
JP25145583A 1983-12-29 1983-12-29 Controlling method of electromagnetic stirring current in continuous casting Granted JPS60145258A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25145583A JPS60145258A (en) 1983-12-29 1983-12-29 Controlling method of electromagnetic stirring current in continuous casting

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25145583A JPS60145258A (en) 1983-12-29 1983-12-29 Controlling method of electromagnetic stirring current in continuous casting

Publications (2)

Publication Number Publication Date
JPS60145258A JPS60145258A (en) 1985-07-31
JPS6358069B2 true JPS6358069B2 (en) 1988-11-14

Family

ID=17223077

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25145583A Granted JPS60145258A (en) 1983-12-29 1983-12-29 Controlling method of electromagnetic stirring current in continuous casting

Country Status (1)

Country Link
JP (1) JPS60145258A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100970245B1 (en) 2007-12-26 2010-07-16 주식회사 포스코아이씨티 Current control method and system of electromagnetic stirrer coil
JP5354179B2 (en) * 2009-03-26 2013-11-27 Jfeスチール株式会社 Continuous casting method for steel slabs

Also Published As

Publication number Publication date
JPS60145258A (en) 1985-07-31

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