JPH0835019A - Electro-slag remelting method - Google Patents

Electro-slag remelting method

Info

Publication number
JPH0835019A
JPH0835019A JP6169194A JP16919494A JPH0835019A JP H0835019 A JPH0835019 A JP H0835019A JP 6169194 A JP6169194 A JP 6169194A JP 16919494 A JP16919494 A JP 16919494A JP H0835019 A JPH0835019 A JP H0835019A
Authority
JP
Japan
Prior art keywords
remelting
consumable electrode
heating
steel ingot
electro
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
JP6169194A
Other languages
Japanese (ja)
Inventor
Toshinori Ishikawa
敏典 石川
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP6169194A priority Critical patent/JPH0835019A/en
Publication of JPH0835019A publication Critical patent/JPH0835019A/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
    • Y02P10/25Process efficiency

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To improve a working efficiency and to uniformize the characteristic of the obtd. steel ingot by heating a consumable electrode and executing an electro-slag remelting operation to increase the melting speed. CONSTITUTION:A copper-made water-cooling crucible 2 is arranged at the upper part of a copper-made water-cooling surface plate 3 on a surface plate pedestal. While advancing the consumable electrode 1 into this crucible 2 through a hanging-down beam 5, the electric discharge is executed between the consumable electrode and molten slag 6, and the consumable electrode is melted from the tip part thereof and the molten metal pool 7 is formed to obtain the remelted steel ingot 10. In the electro-slag remelting method, the consumable electrode 1 is heated by an induction heating coil 8 fitted to the tip part thereof. By this constitution, the neighborhood of tip part of the consumable electrode under room temp. condition is heated at the starting time of remelting, and further, the heating is continued on the way of remelting, too, and the melting speed is increased at the same time of starting the remelting. Further, the remelted steel ingot having uniform characteristic can be obtd. by executing the controlling beating together with cont rolling the voltage and the current for discharging.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はエレクトロスラグ再溶解
法に関する。
FIELD OF THE INVENTION The present invention relates to an electroslag remelting method.

【0002】[0002]

【従来の技術】清浄度に優れ、且つ、均一な性状の鋼か
らなる鋼塊を得る一手段としてエレクトロスラグ再溶解
法を用いることは公知の事実であり、従来技術の概要を
図1に示す。この方式は銅製水冷るつぼ2が移動する方
式(再溶解の進行に伴い銅製水冷るつぼ2が上方に移動
し、消耗電極1が下方に移動する方式)によるエレクト
ロスラグ再溶解法で示しているが、再溶解しようとする
消耗電極1が常温状態にあるため再溶解開始時の溶解速
度はそれ以降の部分での再溶解速度より遅いのが実状で
あり、再溶解開始時の作業効率はそれ以降の再溶解の作
業効率より劣る。そしてまた再溶解開始後は再溶解部か
らの伝導熱と消耗電極1が次第に短くなることによる力
率の向上のため、再溶解速度は次第に増す。このため、
電流と電圧だけで溶解速度を制御することは極めて難し
かった。これらは作業効率上、また、できるだけ均一な
鋼塊10を得ようとする上からも好ましいことではなか
った。
2. Description of the Related Art It is a known fact that the electroslag remelting method is used as a means for obtaining a steel ingot having excellent cleanliness and uniform properties, and an outline of the prior art is shown in FIG. . This method is shown by an electroslag remelting method in which the copper water-cooled crucible 2 moves (the copper water-cooled crucible 2 moves upward and the consumable electrode 1 moves downward as the remelting progresses). Since the consumable electrode 1 to be redissolved is at room temperature, the dissolution rate at the start of remelting is actually slower than the remelting rate at the subsequent parts, and the work efficiency at the start of remelting is later. Inferior to redissolving work efficiency. Further, after the start of remelting, the remelting rate gradually increases due to conduction heat from the remelting portion and the power factor improvement due to the consumable electrode 1 becoming shorter. For this reason,
It was extremely difficult to control the dissolution rate only by the current and voltage. These are not preferable in terms of work efficiency and also in order to obtain the steel ingot 10 that is as uniform as possible.

【0003】[0003]

【発明が解決しようとする課題】本発明は再溶解開始時
及びその後の溶解速度を増すことで作業効率を改善し、
また、できるだけ均一な性状の鋼塊に近付けようとする
ものである。
The present invention improves work efficiency by increasing the dissolution rate at the start of re-dissolution and thereafter.
Moreover, it is intended to approach a steel ingot having a property as uniform as possible.

【0004】[0004]

【課題を解決するための手段】再溶解開始時の溶解速度
を増すことで再溶解開始時の作業効率をそれ以降の再溶
解の作業効率に近付け、また、できるだけ均一な性状の
鋼塊に近付けるには、常温状態にある消耗電極の再溶解
開始側先端付近を加熱すること及びその後の再溶解途中
でも消耗電極を加熱することで解決することができる。
[Means for Solving the Problems] By increasing the melting rate at the start of remelting, the work efficiency at the start of remelting can be made closer to the work efficiency of subsequent remelting, and can also be made as close as possible to a steel ingot of uniform properties. Can be solved by heating the vicinity of the tip of the consumable electrode on the side of remelting at room temperature and heating the consumable electrode even during the subsequent remelting.

【0005】[0005]

【作用】常温状態にある消耗電極の再溶解開始側先端付
近を加熱することで、従来であれば消耗電極の再溶解開
始側先端付近の温度が上昇するに要していた時間が短縮
される作用をもたらし、かつ、再溶解開始後、この先端
付近の温度が消耗電極のそれ以降の部分への伝導を速め
る作用をももたらす。さらに、再溶解途中でも消耗電極
を加熱することでその後の再溶解速度を増す作用をす
る。これにより作業効率を向上させ、かつ、再溶解速度
の制御が電流と電圧だけに頼ることなく、この消耗電極
への加熱制御も可能となるので、できるだけ均一な性状
の鋼塊を得ようとするエレクトロスラグ再溶解法の目的
に近付ける作用をもたらす。
By heating the vicinity of the remelting start side tip of the consumable electrode in the room temperature state, the time required for the temperature near the remelting start side tip of the consumable electrode to rise in the conventional case can be shortened. After the start of remelting, the temperature near this tip also has the effect of accelerating the conduction to the subsequent parts of the consumable electrode. Furthermore, by heating the consumable electrode even during remelting, it has the effect of increasing the remelting rate thereafter. This improves the work efficiency, and the control of the remelting rate can be controlled by heating the consumable electrode without relying only on the current and voltage, so that the steel ingot with a property as uniform as possible is to be obtained. It brings about the effect of approaching the purpose of the electroslag remelting method.

【0006】[0006]

【実施例】以下、図を用いて一実施例を示す。Embodiment An embodiment will be described below with reference to the drawings.

【0007】図2は図1の従来技術に用いられる消耗電
極1を加熱する実施例を示したものである。この実施例
では誘導加熱コイル8により加熱する方式を示している
が、他の加熱方式、例えば、火炎加熱等による方式を用
いてもなんら支障はない。本実施例が誘導加熱コイル8
による加熱方式を適用したのは、溶解速度が上昇しすぎ
る状態に達した時、あるいは、上昇しすぎる状態に達す
ることが予想される時はこの加熱を停止し、溶解速度が
下降しすぎる状態に達した時、あるいは下降しすぎる状
態に達することが予想される時はこの加熱を再開するこ
とがそれぞれ容易なことによるものである。
FIG. 2 shows an embodiment for heating the consumable electrode 1 used in the prior art of FIG. In this embodiment, a method of heating with the induction heating coil 8 is shown, but there is no problem even if another heating method, for example, a method of flame heating is used. In this embodiment, the induction heating coil 8 is used.
The heating method is applied when the dissolution rate reaches an excessively high rate, or when it is expected that it will reach an excessively high rate, this heating is stopped and the dissolution rate becomes too low. This is because it is easy to restart the heating when the temperature is reached or when it is expected that the temperature will drop too low.

【0008】[0008]

【発明の効果】図3に、再溶解開始初期の1時間までを
別として、以降の再溶解時の電流と電圧を一定のままで
の条件下による図2で示した一実施例での本発明の効果
を従来技術との比較で示す。縦軸が単位時間当たりの再
溶解量を、横軸が再溶解開始時からの経過時間を、実線
10が本発明による単位時間当たりの再溶解量を、そし
て点線11が従来技術による単位時間当たりの再溶解量
をそれぞれ示している。本実施例では再溶解開始2時間
経過後に消耗電極の加熱を停め、同3時間経過後に加熱
を再開、同5.5 時間経過後に加熱を停めた結果であ
る。
The effect of the present invention is shown in FIG. 3, except for the first hour before the start of re-dissolution, under the condition that the current and voltage at the time of subsequent re-dissolution remain constant in FIG. The effect of the invention will be shown in comparison with the prior art. The vertical axis represents the redissolved amount per unit time, the horizontal axis represents the elapsed time from the start of redissolution, the solid line 10 represents the redissolved amount per unit time according to the present invention, and the dotted line 11 represents the conventional unit per unit time. The redissolved amount of each is shown. In this example, the heating of the consumable electrode was stopped 2 hours after the start of remelting, the heating was restarted 3 hours later, and the heating was stopped 5.5 hours later.

【0009】すなわち、本発明の方法によれば再溶解開
始時から約11時間経過後まで従来技術より単位時間当
たりの再溶解量を約6ないし1kgと大幅に増加させるこ
とが可能となり、従来技術では15時間を要していた全
再溶解時間を3時間短縮させることが可能となった。こ
の結果、生産効率を約20%改善することができ、目的
とした再溶解開始初期での遅い溶解速度を改善でき、で
きるだけ均一な性状の鋼塊を得たいとするエレクトロス
ラグ再溶解法本来の目的を大幅に進めることが可能とな
り、従来電流,電圧の制御で再溶解速度を一定に保とう
とすることは難しいことであったものが極めて容易にな
った。
That is, according to the method of the present invention, the amount of redissolved per unit time can be greatly increased to about 6 to 1 kg from the prior art until about 11 hours after the start of redissolution, and the prior art It was possible to shorten the total re-dissolution time, which required 15 hours, by 3 hours. As a result, the production efficiency can be improved by about 20%, the slow melting rate at the beginning of the intended remelting can be improved, and the ingot of the electroslag remelting method which is intended to obtain a steel ingot with a property as uniform as possible is desired. It has become possible to greatly advance the purpose, and it became extremely easy to control the current and voltage in the past to keep the remelting rate constant.

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

【図1】エレクトロスラグ再溶解法の従来技術を示す説
明図。
FIG. 1 is an explanatory view showing a conventional technique of an electroslag remelting method.

【図2】消耗電極を加熱する一実施例の説明図。FIG. 2 is an explanatory diagram of an example of heating a consumable electrode.

【図3】電流と電圧を一定のままでの条件下による本発
明と従来技術での単位時間当たりの再溶解量を比較した
グラフ。
FIG. 3 is a graph comparing the amount of redissolution per unit time between the present invention and the prior art under the condition that the current and voltage are kept constant.

【符号の説明】[Explanation of symbols]

1…消耗電極、2…銅製水冷るつぼ、3…銅製水冷定
盤、4…定盤台座、5…電極懸下アーム、6…溶融スラ
グ、7…溶湯プール、8…誘導加熱コイル、9…冷却
水、10…再溶解量。
1 ... Consumable electrode, 2 ... Copper water-cooled crucible, 3 ... Copper water-cooled surface plate, 4 ... Surface plate base, 5 ... Electrode suspension arm, 6 ... Molten slag, 7 ... Molten pool, 8 ... Induction heating coil, 9 ... Cooling Water, 10 ... Redissolved amount.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】エレクトロスラグ再溶解法において消耗電
極を加熱することでを特徴とするエレクトロスラグ再溶
解方法。
1. An electroslag remelting method comprising heating a consumable electrode in the electroslag remelting method.
JP6169194A 1994-07-21 1994-07-21 Electro-slag remelting method Pending JPH0835019A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6169194A JPH0835019A (en) 1994-07-21 1994-07-21 Electro-slag remelting method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6169194A JPH0835019A (en) 1994-07-21 1994-07-21 Electro-slag remelting method

Publications (1)

Publication Number Publication Date
JPH0835019A true JPH0835019A (en) 1996-02-06

Family

ID=15881966

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6169194A Pending JPH0835019A (en) 1994-07-21 1994-07-21 Electro-slag remelting method

Country Status (1)

Country Link
JP (1) JPH0835019A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013032703A3 (en) * 2011-08-26 2013-05-10 Consarc Corporation Purification of a metalloid by consumable electrode vacuum arc remelt process
CN103409640A (en) * 2013-08-07 2013-11-27 武汉重工铸锻有限责任公司 Gantry frame type dual-furnace-end three-station interchangeable smelting electric slag furnace with driven-out crystallizer vehicle
CN104878214A (en) * 2015-05-14 2015-09-02 浙江天马轴承有限公司 Electro slag ingot casting device adopting molten steel shunt and gas protection
CN105290378A (en) * 2014-07-17 2016-02-03 厦门华海大正电池装备有限公司 Cast-welding method for lead-acid storage battery tabs
CN108247021A (en) * 2018-04-04 2018-07-06 安徽工业大学 A kind of electroslag remelting device and its method for preheating consutrode production composite roll
CN108273980A (en) * 2018-04-04 2018-07-13 安徽工业大学 A kind of preheating consutrode electroslag remelting production composite roll method

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013032703A3 (en) * 2011-08-26 2013-05-10 Consarc Corporation Purification of a metalloid by consumable electrode vacuum arc remelt process
KR20140059823A (en) * 2011-08-26 2014-05-16 콘삭 코퍼레이션 Purification of a metalloid by consumable electrode vacuum arc remelt process
JP2014529568A (en) * 2011-08-26 2014-11-13 コンサーク コーポレイションConsarc Corporation Purification of metalloid by consumable electrode vacuum arc remelting method
US9340896B2 (en) 2011-08-26 2016-05-17 Consarc Corporation Purification of a metalloid by consumable electrode vacuum arc remelt process
CN103409640A (en) * 2013-08-07 2013-11-27 武汉重工铸锻有限责任公司 Gantry frame type dual-furnace-end three-station interchangeable smelting electric slag furnace with driven-out crystallizer vehicle
CN105290378A (en) * 2014-07-17 2016-02-03 厦门华海大正电池装备有限公司 Cast-welding method for lead-acid storage battery tabs
CN104878214A (en) * 2015-05-14 2015-09-02 浙江天马轴承有限公司 Electro slag ingot casting device adopting molten steel shunt and gas protection
CN108247021A (en) * 2018-04-04 2018-07-06 安徽工业大学 A kind of electroslag remelting device and its method for preheating consutrode production composite roll
CN108273980A (en) * 2018-04-04 2018-07-13 安徽工业大学 A kind of preheating consutrode electroslag remelting production composite roll method

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