JPH0820827A - Electro-slag remelting method - Google Patents

Electro-slag remelting method

Info

Publication number
JPH0820827A
JPH0820827A JP6155650A JP15565094A JPH0820827A JP H0820827 A JPH0820827 A JP H0820827A JP 6155650 A JP6155650 A JP 6155650A JP 15565094 A JP15565094 A JP 15565094A JP H0820827 A JPH0820827 A JP H0820827A
Authority
JP
Japan
Prior art keywords
remelting
electrode
tip part
consumable electrode
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
JP6155650A
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 JP6155650A priority Critical patent/JPH0820827A/en
Publication of JPH0820827A publication Critical patent/JPH0820827A/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 the working efficiency at the initial stage of remelting and to uniformize the characteristic of an obtd. steel ingot by preheating the tip part of a consumable electrode at the initial stage of the remelting by using an electro-slag remelting method. CONSTITUTION:At the time of producing the steel ingot having excellent cleanliness and uniform characteristic by using the electro-slag remelting method, the steel-made consumable electrode 1 as the raw material is fit to a turnable arm 5 for hanging down the electrode and then, an induction heating coil 8 is fit to the tip part of the electrode 1, and the electric current is conducted to the coil 8 to heat the tip part of the electrode 1 by the induction current. Melting rate of the tip part of the electrode 1 becomes large at the initial stage of the remelting refining of the consumable electrode by this heating, and the whole melting time of the electrode 1 can be shortened, and the steel ingot having excellent uniformity is obtd. by remelting under the excellent working efficiency.

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、これから再溶解しよ
うとする消耗電極1は常温状態にあるため再溶解開始初
期時の溶解速度はそれ以降の部分での再溶解速度より遅
いのが実状である。これは、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
率の向上作用により再溶解速度が次第に増す事によるた
めである。このため、再溶解開始初期時の作業効率はそ
れ以降の再溶解の作業効率より劣り、また、できるだけ
均一な鋼塊10を得ようとする上で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 from now on is at room temperature, the actual dissolution rate at the beginning of the remelting is slower than the remelting rate in the subsequent portions. This is because after the start of remelting, the heat of conduction from the remelting portion and the consumable electrode 1 are gradually shortened to gradually increase the remelting rate due to the power factor improving action. Therefore, the work efficiency at the beginning of remelting is inferior to the work efficiency of the subsequent remelting, and it is not preferable in order to obtain the steel ingot 10 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初
期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ようとするものである。
DISCLOSURE OF THE INVENTION The present invention makes the work efficiency at the start of re-dissolution close to the work efficiency of subsequent re-dissolution by increasing the dissolution rate at the initial stage of the start of re-dissolution, and it is possible to obtain a property as uniform as possible. It tries to get closer to the steel ingot.

【0004】[0004]

【課題を解決するための手段】再溶解開始初期時の溶解
速度を増すことで再溶解開始初期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予熱することで解決すること
ができる。
[Means for Solving the Problems] By increasing the dissolution rate at the beginning of remelting, the work efficiency at the beginning of remelting can be brought closer to the work efficiency of the subsequent remelting, and a steel ingot with as uniform a property as possible To solve the problem, it is possible to solve the problem by preheating the vicinity of the tip of the remelting start side of the consumable electrode at room temperature.

【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
近を予熱することで、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。
By preheating the vicinity of the remelting start side tip of the consumable electrode in the normal 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.

【0006】[0006]

【実施例】以下、図を用いて一実施例を示す。図2は図
1の従来技術に用いられる消耗電極1を旋回可能な電極
懸下アーム5に取り付けたのち、この消耗電極1の下
方、すなわち、再溶解開始側の電極先端付近を予熱する
実施例を示したものである。この実施例では再溶解開始
側の電極1の先端付近を誘導加熱コイル8により予熱す
る方式を示しているが、他の加熱方式、例えば、火炎加
熱,炉加熱による方式を用いてもなんら支障はない。本
予熱を実施したのち、電極懸下アーム5を旋回させてあ
らかじめ溶解の準備がなされている銅製水冷るつぼ2に
セットして再溶解を開始する。
Embodiment An embodiment will be described below with reference to the drawings. FIG. 2 shows an embodiment in which the consumable electrode 1 used in the prior art shown in FIG. 1 is attached to a swivel electrode suspension arm 5, and then the consumable electrode 1 is preheated below the consumable electrode 1, that is, near the electrode tip on the remelting start side. Is shown. In this embodiment, a method of preheating the vicinity of the tip of the electrode 1 on the remelting start side by the induction heating coil 8 is shown, but there is no problem even if another heating method such as flame heating or furnace heating is used. Absent. After the main preheating is performed, the electrode suspension arm 5 is swung to set in the copper water-cooled crucible 2 which is prepared for melting in advance, and remelting is started.

【0007】[0007]

【発明の効果】図3に再溶解開始直後の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1
1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12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。
The present invention in one embodiment shown in FIG. 2 under the condition that the current and voltage during the subsequent remelting are kept constant except for 1 hour immediately after the start of remelting in FIG. The effect of is compared with the prior art. The vertical axis represents the amount of redissolution per unit time, the horizontal axis represents the elapsed time from the start of redissolution, and the solid line 1
1 shows the redissolved amount per unit time according to the present invention, and the dotted line 12 shows the redissolved amount per unit time according to the prior art.

【0008】すなわち、本発明の方法によれば再溶解開
始時から約4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2kg増加させることが可能となり、こ
の増加分は次第に減じるものの、従来技術では15時間
を要していた全再溶解時間を1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7%改善すること
が可能にできるとともに、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ることにあわせ、できるだけ
均一な性状の鋼塊10を得たいとするエレクトロスラグ
再溶解法で本来の目的をさらに進めることが可能となっ
た。
That is, according to the method of the present invention, it becomes possible to increase the amount of redissolved per unit time by about 2 kg from the start of redissolution until about 4 hours have elapsed, and this increased amount is gradually reduced. The total re-dissolution time, which required 15 hours in the conventional technique, can be shortened by 1 hour. As a result, it is possible to improve the production efficiency by about 7% and to improve the slow melting rate at the initial stage of the start of remelting, which is aimed at obtaining a steel ingot 10 having a property as uniform as possible. The slag remelting method made it possible to further the original purpose.

【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】消耗電極の再溶解開始側先端付近を予熱する一
実施例の説明図。
FIG. 2 is an explanatory diagram of an embodiment in which the vicinity of the tip of the consumable electrode on the remelting start side is preheated.

【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
特性図。
FIG. 3 is a characteristic diagram 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…鋼塊、11,12…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 ... Steel ingot, 11, 12 ... 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溶解初
期部に相当する消耗電極の先端付近を予熱することで再
溶解開始初期時の溶解速度を改善することを特徴とする
エレクトロスラグ再溶解方法。
1. An electroslag remelting method, characterized in that in the electroslag remelting method, the vicinity of the tip of a consumable electrode corresponding to the initial portion of melting is preheated to improve the dissolution rate at the beginning of remelting.
JP6155650A 1994-07-07 1994-07-07 Electro-slag remelting method Pending JPH0820827A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6155650A JPH0820827A (en) 1994-07-07 1994-07-07 Electro-slag remelting method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6155650A JPH0820827A (en) 1994-07-07 1994-07-07 Electro-slag remelting method

Publications (1)

Publication Number Publication Date
JPH0820827A true JPH0820827A (en) 1996-01-23

Family

ID=15610605

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6155650A Pending JPH0820827A (en) 1994-07-07 1994-07-07 Electro-slag remelting method

Country Status (1)

Country Link
JP (1) JPH0820827A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20140059823A (en) * 2011-08-26 2014-05-16 콘삭 코퍼레이션 Purification of a metalloid by consumable electrode vacuum arc remelt process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Similar Documents

Publication Publication Date Title
JPH0835019A (en) Electro-slag remelting method
JPH0820827A (en) Electro-slag remelting method
US3978907A (en) Method of electroslag remelting by melting main and additional electrodes and machine for effecting said method
US3759311A (en) Arc slag melting
JP2004522852A (en) Method for producing metal ingot or billet by melting electrodes in conductive slag bath and apparatus for performing the same
US3565994A (en) Electrode slag melting method
JPH0452067A (en) Production of cast ingot
CN113667831B (en) Electroslag remelting device and method for refining electroslag ingot solidification structure through dual power supply coupling
JPH05285632A (en) Method for electrically melting slag
RU2016132025A (en) A method of manufacturing a bimetallic electrode by electroslag surfacing and a method of utilizing metallurgical slag by reduction smelting using a bimetallic electrode
SU729253A2 (en) Method of vacuum arc smelting of steels and alloys
JP2008178908A (en) Process for electroslag remelting of metal and ingot mold used therefor
SU642966A1 (en) Method of electroslag remelting of profiled ingots
JP2000301320A (en) Method for dissolving clogging of porous plug in ladle refining furnace
JP2006257515A (en) Ingot manufacturing method, and tool for cold starting
SU1693102A1 (en) Electro-slag smelting apparatus
JPS62266384A (en) Arc furnace for steel manufacture
KR100694332B1 (en) Bottom pour electroslag refining systems and methods
RU2124963C1 (en) Process of reconditioning of parts by pouring with liquid metal
JP2949697B2 (en) Cast iron manufacturing method
JP2001289567A (en) Control method for induction furnace
RU2038424C1 (en) Method for preparation of blooms for mounting in cathode section of aluminium electrolyzer
RU2244029C2 (en) Method of production of ingots
JP2946623B2 (en) DC arc furnace
JP2001262245A (en) Apparatus and method for refining bottom-pouring type electroslag