JP2007302954A - Method for electrically remelting slag in vacuum and apparatus for electrically remelting slag in vacuum - Google Patents

Method for electrically remelting slag in vacuum and apparatus for electrically remelting slag in vacuum Download PDF

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JP2007302954A
JP2007302954A JP2006133131A JP2006133131A JP2007302954A JP 2007302954 A JP2007302954 A JP 2007302954A JP 2006133131 A JP2006133131 A JP 2006133131A JP 2006133131 A JP2006133131 A JP 2006133131A JP 2007302954 A JP2007302954 A JP 2007302954A
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slag
furnace
electroslag remelting
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Naoki Ichikawa
直毅 市川
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Daido Steel Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for electrically remelting slag in a vacuum, which can conduct an operation by using such a slag as to have a low melting point, be easily melted and be able to decrease the amount of oxide inclusions while avoiding the boiling of the slag, and to provide an apparatus therefor. <P>SOLUTION: This slag-remelting method includes refining a metal in a degree of vacuum in a range of 100 to 600 Torr by using a slag containing 20 to 80 wt.% CaF<SB>2</SB>and the balance mainly CaO and (or) Al<SB>2</SB>O<SB>3</SB>, while maintaining a threshold pressure condition at which the slag does not substantially start boiling. The degree of the vacuum in a furnace is adjusted by concurrently exhausting air with a vacuum pump and injecting argon gas in the furnace. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、真空エレクトロスラグ再溶解法の改良に関し、その方法の実施に使用する装置にも関する。 The present invention relates to improvements in the vacuum electroslag remelting process and also relates to the apparatus used to carry out the process.

よく知られているように、エレクトロスラグ再溶解法は、大気中または不活性ガス雰囲気下で、溶融スラグのジュール熱により消耗電極を溶解し、銅製の水冷鋳型内で積層凝固させる再溶解技術である。詳しくは、水冷鋳型中で、溶融したスラグの上方に配置した、精錬しようとする金属、主として鋼からなる消耗電極と、下方にあって積層凝固した鋼塊との間に通電し、溶融して消耗電極からしたたり落ちる金属の液滴が溶融スラグ中を通過する間に精錬する技術である。 As is well known, electroslag remelting is a remelting technique in which consumable electrodes are melted by the Joule heat of molten slag in the air or under an inert gas atmosphere, and laminated and solidified in a copper water-cooled mold. is there. Specifically, in a water-cooled mold, an electric current is passed between a consumable electrode made of a metal to be refined, mainly steel, located above the molten slag, and a steel ingot that is laminated and solidified at the lower side. This is a technique in which metal droplets dripping or dropping from a consumable electrode are refined while passing through a molten slag.

大気雰囲気下のエレクトロスラグ再溶解は、設備に関する要求が緩やかであり、操業も容易であるが、スラグの劣化に伴う精錬能力、とくに脱酸性能の低下が避けられないし、大気中の水分や窒素のピックアップにより水素欠陥や窒化物の生成という問題がある。精錬にともない溶鋼中の活性成分が失われ、合金組成のバラツキが起こることも、大気雰囲気下のエレクトロスラグ再溶解の弱点である。 Electroslag remelting in the atmosphere is less demanding on equipment and easy to operate, but the refining capacity, particularly deoxidation performance, associated with slag deterioration is unavoidable, and it is difficult to avoid moisture and nitrogen in the atmosphere. There is a problem of generation of hydrogen defects and nitrides due to the pickup. The active component in the molten steel is lost as a result of refining, and variations in the alloy composition occur. This is a weak point of electroslag remelting in the atmosphere.

こうした問題を解消した製錬技術として、精錬雰囲気を減圧下に置く、真空エレクトロスラグ再溶解法が行なわれる。基本的な技術は、「金属のエレクトロスラグ再溶融法」として開示された方法であって、a)再溶融工程を減圧(具体的には200〜10-2mbar)下に実施、b)スラグとして少なくとも80重量%が沸点2000℃を上回る酸化物からなるものを使用し、かつ、c)交流加熱を行なうこと、を特徴とする(特許文献1)。 As a smelting technique that solves these problems, a vacuum electroslag remelting method is performed in which a smelting atmosphere is placed under reduced pressure. The basic technique is the method disclosed as “metal electroslag remelting method”, wherein a) the remelting step is carried out under reduced pressure (specifically 200 to 10 −2 mbar), b) slag Using at least 80% by weight of an oxide having a boiling point higher than 2000 ° C., and c) performing AC heating (Patent Document 1).

出願人は、真空エレクトロスラグ再溶解法に関し、「成分制御真空ESR方法」として、極性を可変とした電極をスラグ中に浸漬して、直流を通電する方法を開示した(特許文献2)。この技術は、極性を利用して、S,Al,Pなどの成分の制御をおこなうことができる。ついで出願人は、「含硫黄鋼材のエレクトロスラグ再溶解法」について、硫化鉄粉末を混合したスラグを使用したESR技術を開発し、これも開示した(特許文献3)。装置に関しても、炉体およびその周辺の構成部品を非磁性とすることにより、電力ロスを低減した「真空エレクトロスラグ再溶解炉」を提案した(特許文献4)。
特開昭63−259031(特許2588895) 特開平3−197624 特開平7−62461 特開平7−238327
Regarding the vacuum electroslag remelting method, the applicant disclosed a method of energizing a direct current by immersing an electrode with variable polarity in the slag as a “component control vacuum ESR method” (Patent Document 2). This technique can control components such as S, Al, and P using polarity. Subsequently, the applicant developed and disclosed an ESR technique using slag mixed with iron sulfide powder for the “electroslag remelting method of sulfur-containing steel” (Patent Document 3). Regarding the apparatus, a “vacuum electroslag remelting furnace” in which the power loss was reduced by making the furnace body and its surrounding components nonmagnetic was proposed (Patent Document 4).
JP 63-259031 (Patent 2588895) JP-A-3-197624 JP-A-7-62461 JP 7-238327 A

前記した基本的な真空エレクトロスラグ再溶解技術に関していえば、「200〜10-2mbar」(0.01〜150Torr)という真空下の操業を円滑に行なうために、「スラグとして少なくとも80重量%が沸点2000℃を上回る酸化物からなるもの」、つまり酸化物主体のスラグを使用せざるを得なかったわけである。しかし、酸化物主体のスラグを使用すると、融点が高くて溶融が容易でないという問題がある。スラグのボイリングという問題が避けられれば、CaF2のような成分をより多量に含んだ、エレクトロスラグ再溶解にとって好都合であり、経済的にも有利な組成のスラグを使用して、再溶解を実施することが望ましい。 Regarding the basic vacuum electroslag remelting technique described above, in order to smoothly operate under a vacuum of “200 to 10 −2 mbar” (0.01 to 150 Torr), “at least 80% by weight as slag is required. That is, an oxide having a boiling point higher than 2000 ° C. ”, that is, an oxide-based slag has to be used. However, when oxide-based slag is used, there is a problem that melting point is high and melting is not easy. If the problem of slag boiling is avoided, remelting is carried out using a slag with a composition that is advantageous for electroslag remelting and contains an economically advantageous composition that contains a larger amount of components such as CaF 2. It is desirable to do.

本発明の目的は、このような要望にこたえ、融点が低く、溶融が容易である上に、介在物の量を低くすることができるようなスラグを使用し、かつ、スラグのボイリングを避けて操業することができるような、真空エレクトロスラグ再溶解の方法を提供することにある。その方法の実施に使用して好適な、真空エレクトロスラグ再溶解装置を提供することも、本発明の目的に含まれる。 The object of the present invention is to meet such demands, use a slag that has a low melting point, is easy to melt, and can reduce the amount of inclusions, and avoids boiling of the slag. The object is to provide a method of vacuum electroslag remelting that can be operated. It is also within the scope of the present invention to provide a vacuum electroslag remelting apparatus suitable for use in carrying out the method.

本発明の真空エレクトロスラグ再溶解法は、真空エレクトロスラグ再溶解炉を用いて金属の精錬を行なう方法であって、CaF2を20〜80重量%含有し、残りが主としてCaOおよび(または)Al23からなるスラグを使用し、真空度が100〜600Torrの範囲内でスラグのボイリングが実質上生じない圧力条件を維持しながら精錬を行なうことを特徴とする方法である。スラグは、上記の成分のほか、MgOなどを含むものであってもよい。 The vacuum electroslag remelting method of the present invention is a method of refining metal using a vacuum electroslag remelting furnace, containing 20 to 80% by weight of CaF 2 , with the remainder mainly CaO and / or Al. This is a method characterized by using slag composed of 2 O 3 and performing refining while maintaining a pressure condition in which slag boiling does not substantially occur within a vacuum range of 100 to 600 Torr. The slag may contain MgO in addition to the above components.

本発明の真空エレクトロスラグ再溶解法は、CaF2を20〜80重量%含有し、残りが主としてCaOおよびAl23からなるスラグを使用するから、その融点は酸化物主体のスラグに比べて低く、溶融が容易である。溶融が容易であるということは、とりもなおさず、プロセスコントロールにとって有利であるということであり、安定した品質の製品を低コストで提供できることを意味する。 Since the vacuum electroslag remelting method of the present invention uses slag containing 20 to 80% by weight of CaF 2 and the remainder mainly composed of CaO and Al 2 O 3 , the melting point thereof is higher than that of slag mainly composed of oxide. Low and easy to melt. The ease of melting means that it is advantageous for process control, and means that stable quality products can be provided at low cost.

本発明の真空エレクトロスラグ再溶解法の実施に適する真空度は、上記した100〜600Torrの範囲内で、スラグ組成、消耗電極の合金組成およびそのサイズなどの因子によって決定される。スラグのボイリングが発生する真空度の限界は、上述の操業条件によってほぼ決定されるから、操業可能な真空度の限界をまず把握することが必要である。当業者は、必要に応じて若干の試験を行なうことにより、その限界を知ることができる。精錬の進行に伴い、スラグ組成に若干の変動が生じることがあれば、それも考慮にして、維持すべき真空度の限界を決定する。 The degree of vacuum suitable for carrying out the vacuum electroslag remelting method of the present invention is determined by factors such as the slag composition, the alloy composition of the consumable electrode and the size thereof within the range of 100 to 600 Torr. Since the limit of the degree of vacuum at which slag boiling occurs is substantially determined by the above-described operating conditions, it is necessary to first understand the limit of the operable vacuum. Those skilled in the art can know the limitations by performing some tests as needed. If the slag composition slightly changes with the progress of refining, the limit of the degree of vacuum to be maintained is determined in consideration of this.

このアルゴンガスの注入による真空度の調節は、真空エレクトロスラグ再溶解の操業開始に当たっても利用できる。すなわち、操業に先だって、炉内を高い真空度に減圧したのちアルゴンガスを注入して真空度を下げ、所望の真空度を実現したのち通電し、精錬を開始するというスタートアップ方法が推奨される。 This adjustment of the degree of vacuum by injecting argon gas can also be used at the start of vacuum electroslag remelting operation. That is, prior to operation, a start-up method is recommended in which the inside of the furnace is depressurized to a high degree of vacuum and then argon gas is injected to lower the degree of vacuum to achieve a desired degree of vacuum and then energize to start refining.

上記した方法を実施するのに適した本発明の真空エレクトロスラグ再溶解装置は、図1に示すように、水冷銅るつぼ(1)とその上部に設けた炉体(2)、真空ポンプ(3)、炉内と真空ポンプとを接続するための、途中にメインバルブ(V1)を備えたメインライン(6)、メインバルブをバイパスする、コントロールバルブ(V2)を備えたバイパスライン(7)、アルゴンガス源(4)と、炉内をアルゴンガス源に接続するための、アルゴンバルブ(V3)を備えたアルゴンライン(8)を本質的な構成要素とし、電源(5)および電極昇降手段(図示してない)を付属させてなる。これに、炉内の真空度を測定する圧力計や温度計など、付帯する設備があることはいうまでもない。 As shown in FIG. 1, the vacuum electroslag remelting apparatus of the present invention suitable for carrying out the above-described method includes a water-cooled copper crucible (1), a furnace body (2) provided thereon, a vacuum pump (3 ), A main line (6) having a main valve (V1) in the middle for connecting the inside of the furnace and the vacuum pump, a bypass line (7) having a control valve (V2) for bypassing the main valve, An argon gas source (4) and an argon line (8) with an argon valve (V3) for connecting the inside of the furnace to the argon gas source are essential components, and a power source (5) and electrode lifting / lowering means ( (Not shown). It goes without saying that there are incidental facilities such as a pressure gauge and a thermometer for measuring the degree of vacuum in the furnace.

この装置の運転は、つぎのように行なう。まず、電極昇降手段を作動させて消耗電極を適切な位置に置き、真空ポンプを運転して炉内を減圧する。このときはメインライン(6)を通して急速に空気を抜き出し、速やかに、予定した真空度より少し低い炉内圧力とするが、微細な制御はバイパスライン(7)のコントロールバルブ(V2)を用いて行なう。つぎにメインライン(6)のメインバルブ(V1)を閉じ、アルゴンライン(8)のアルゴンバルブ(V3)を開いてアルゴンガスを炉内に注入し、所望の真空度を実現する。 The operation of this apparatus is performed as follows. First, the electrode raising / lowering means is operated to place the consumable electrode at an appropriate position, and the vacuum pump is operated to depressurize the inside of the furnace. At this time, the air is rapidly extracted through the main line (6), and the pressure inside the furnace is set to be slightly lower than the expected vacuum level. However, fine control is performed using the control valve (V2) of the bypass line (7). Do. Next, the main valve (V1) of the main line (6) is closed, the argon valve (V3) of the argon line (8) is opened, and argon gas is injected into the furnace to achieve a desired degree of vacuum.

所望の真空度に至ったところで水冷銅るつぼ内に適量のスラグ組成物を入れ、通電してスラグを溶融させるとともに、消耗電極から金属液滴を落下させ、それがスラグ中を通過する間に精錬されるようにして、真空エレクトロスラグ再溶解を実施する。通電は、交流によることも、直流によることもできる。精錬中は、炉内の真空度の維持に必要な限度で、真空ポンプを運転する。炉内の状況は、圧力計により、また必要によりのぞき窓を通しての観察により、把握する。 When a desired degree of vacuum is reached, an appropriate amount of slag composition is placed in a water-cooled copper crucible, and the slag is melted by energization, and metal droplets are dropped from the consumable electrode and refined while it passes through the slag. Perform vacuum electroslag remelting as described. The energization can be either alternating current or direct current. During refining, the vacuum pump is operated to the limit necessary to maintain the degree of vacuum in the furnace. The condition in the furnace is grasped by a pressure gauge and, if necessary, by observation through a viewing window.

重量割合で、CaF2:70%、Al23:30%からなるスラグを用意した。図1のように構成した、最大容量1750KVAの装置を使用して、ステンレス鋼の真空エレクトロスラグ再溶解を実施した。スタートは、真空ポンプの運転によりいったんは約0.1Torrの真空度とした後、アルゴンガスを注入して真空度を150Torrに戻し、交流電流を流して精錬を開始した。炉内の圧力を連続的に観測し、必要に応じて真空ポンプを運転し、炉内の真空度を120〜180Torrの範囲内、平均150Torrに維持して、セットした消耗電極が溶解する約5時間の間、運転を続けた。この間、スラグのボイリングは観察されなかった。水冷銅るつぼ内に凝固したインゴットは、H:2ppm、O:20ppm、N:350ppmと、純度の高い清浄なものであった。 A slag composed of CaF 2 : 70% and Al 2 O 3 : 30% by weight was prepared. Stainless steel vacuum electroslag remelting was performed using an apparatus configured as shown in FIG. 1 and having a maximum capacity of 1750 KVA. The start was that the degree of vacuum was once about 0.1 Torr by operating the vacuum pump, and then argon gas was injected to return the degree of vacuum to 150 Torr, and an alternating current was applied to start refining. The pressure in the furnace is continuously observed, the vacuum pump is operated as necessary, the vacuum in the furnace is maintained within the range of 120 to 180 Torr, and an average of 150 Torr, and the set consumable electrode is dissolved. He continued driving for hours. During this time, no slag boiling was observed. The ingot solidified in the water-cooled copper crucible was clean with high purity of H: 2 ppm, O: 20 ppm and N: 350 ppm.

本発明の真空エレクトロスラグ再溶解装置の構成を示す、主要部の配置図。The layout of the principal part which shows the structure of the vacuum electroslag remelting apparatus of this invention.

符号の説明Explanation of symbols

1 水冷銅るつぼ
2 炉体
3 真空ポンプ
4 アルゴンガス源
5 電源
6 メインライン
7 バイパスライン
8 アルゴンライン
V1 メインバルブ
V2 コントロールバルブ
V3 アルゴンバルブ


1 Water-cooled copper crucible 2 Furnace 3 Vacuum pump 4 Argon gas source 5 Power supply 6 Main line 7 Bypass line 8 Argon line V1 Main valve V2 Control valve V3 Argon valve


Claims (3)

真空エレクトロスラグ再溶解炉を用いて金属の精錬を行なう方法であって、CaF2を20〜80重量%含有し、残りが主としてCaOおよび(または)Al23からなるスラグを使用し、真空度が100〜600Torrの範囲内でスラグのボイリングが実質上生じない圧力条件を維持しながら精錬を行なうことを特徴とする真空エレクトロスラグ再溶解法。 A method of refining metal using a vacuum electroslag remelting furnace, comprising 20 to 80% by weight of CaF 2 , and using a slag mainly composed of CaO and / or Al 2 O 3 A vacuum electroslag remelting method characterized in that refining is performed while maintaining a pressure condition in which boiling of slag does not substantially occur within a range of 100 to 600 Torr. 操業開始に当たり、高い真空度に減圧したのちアルゴンガスを注入して真空度を下げ、所望の真空度を実現したのち通電し、精錬を開始することからなる請求項1に記載した真空エレクトロスラグ再溶解法のスタートアップ方法。 2. The vacuum electroslag re-starting according to claim 1, comprising depressurizing to a high degree of vacuum, injecting argon gas to lower the degree of vacuum, realizing a desired degree of vacuum, and energizing to start refining. Start-up method of dissolution method. 水冷銅るつぼ(1)とその上部に設けた炉体(2)、真空ポンプ(3)、炉内と真空ポンプとを接続するための、途中にメインバルブ(V1)を備えたメインライン(6)、メインバルブをバイパスする、コントロールバルブ(V2)を備えたバイパスライン(7)、アルゴンガス源(4)と、炉内をアルゴンガス源に接続するための、アルゴンバルブ(V3)を備えたアルゴンライン(8)を本質的な構成要素とし、電源(5)および電極昇降手段(図示してない)を付属させてなる真空エレクトロスラグ再溶解装置。
A water-cooled copper crucible (1) and a furnace body (2) provided on the upper part thereof, a vacuum pump (3), and a main line (6) provided with a main valve (V1) in the middle for connecting the furnace and the vacuum pump. ), Bypass line (7) with control valve (V2) bypassing the main valve, argon gas source (4), and argon valve (V3) for connecting the inside of the furnace to the argon gas source A vacuum electroslag remelting apparatus comprising an argon line (8) as an essential component and a power source (5) and electrode lifting / lowering means (not shown).
JP2006133131A 2006-05-11 2006-05-11 Method for electrically remelting slag in vacuum and apparatus for electrically remelting slag in vacuum Pending JP2007302954A (en)

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JP2013507531A (en) * 2009-10-12 2013-03-04 スネクマ Degassing of martensitic stainless steel before electroslag remelting
CN102002599A (en) * 2010-11-15 2011-04-06 成都天马铁路轴承有限公司 Vacuum argon-filling pressurizing electroslag remelting method
CN104313340A (en) * 2014-10-31 2015-01-28 山西太钢不锈钢股份有限公司 Electroslag smelting method for TWZ-2 steel
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CN107312937A (en) * 2017-06-26 2017-11-03 洛阳双瑞特种装备有限公司 A kind of the high temperature resistant concentrated sulfuric acid high silicon stainless steel manufacture method and its equipment
CN108866345A (en) * 2018-07-27 2018-11-23 东北大学 A kind of vacuum electroslag remelting furnace melting high-cleanness, high steel ingot method
CN109112319A (en) * 2018-09-18 2019-01-01 重庆材料研究院有限公司 Slag charge for nuclear grade stainless steel electroslag remelting and the method using slag charge progress electroslag remelting
CN109112319B (en) * 2018-09-18 2020-11-10 重庆材料研究院有限公司 Slag for nuclear-grade stainless steel electroslag remelting and method for electroslag remelting by using slag
WO2021033692A1 (en) * 2019-08-19 2021-02-25 デンカ株式会社 Premelted flux
JP2021030247A (en) * 2019-08-19 2021-03-01 山陽特殊製鋼株式会社 Premelt flux for electroslag remelting method
JP7385401B2 (en) 2019-08-19 2023-11-22 山陽特殊製鋼株式会社 Premelt flux for electroslag remelting process
CN110640120A (en) * 2019-10-30 2020-01-03 上海电气上重铸锻有限公司 Manufacturing device and manufacturing method of stainless steel electroslag remelting steel ingot
CN113088716A (en) * 2021-03-31 2021-07-09 安徽富凯特材有限公司 Ultralow-oxygen slag system for electroslag remelting and preparation method thereof
CN115786800A (en) * 2022-11-28 2023-03-14 苏州大学 Smelting device for clean homogenized extra-large steel ingot and using method
CN115786800B (en) * 2022-11-28 2024-05-28 苏州大学 Smelting device for clean homogenized oversized steel ingot and use method

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