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JPS6115786B2 - - Google Patents
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JPS6115786B2 - - Google Patents

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Publication number
JPS6115786B2
JPS6115786B2 JP54057024A JP5702479A JPS6115786B2 JP S6115786 B2 JPS6115786 B2 JP S6115786B2 JP 54057024 A JP54057024 A JP 54057024A JP 5702479 A JP5702479 A JP 5702479A JP S6115786 B2 JPS6115786 B2 JP S6115786B2
Authority
JP
Japan
Prior art keywords
melting
metals
raw material
recycled raw
alloys
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
JP54057024A
Other languages
Japanese (ja)
Other versions
JPS55149770A (en
Inventor
Chikara Hayashi
Seiichiro Kashu
Yoshuki Yoneda
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.)
Vacuum Metallurgical Co Ltd
Original Assignee
Vacuum Metallurgical Co 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 Vacuum Metallurgical Co Ltd filed Critical Vacuum Metallurgical Co Ltd
Priority to JP5702479A priority Critical patent/JPS55149770A/en
Publication of JPS55149770A publication Critical patent/JPS55149770A/en
Publication of JPS6115786B2 publication Critical patent/JPS6115786B2/ja
Granted legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は活性金属又は高融点金属或はそれら合
金の粗インゴツトを造塊する方法に関する。 高融点金属および活性金属は省資源の立場か
ら、造塊、加工などのプロセスで発生したスクラ
ツプもしくは製品として使用され、寿命もしくは
不用などのため使用しないスクラツプの再生が近
年強く望まれている。 これら金属及び合金それぞれの製造工程および
使用先で発生したスクラツプのうち再生可能のも
の(以下再生原料とよぶ)を高真空中もしくは高
純度不活性ガスで置換された低圧真空中で再溶解
し、造塊することが知られている。 これら公知の溶解・造塊方法としては、パージ
ン原料の溶解と同様に電子ビーム(高電圧)溶
解、真空アーク(低電圧)溶解、不活性ガス雰囲
気におけるアーク(低電圧)溶解及びプラズマ溶
解等の手段が主に用いられている。 高融点・活性金属の合金の代表例を挙げると表
−1の通りである。
The present invention relates to a method for forming crude ingots of active metals or refractory metals or their alloys. From the standpoint of resource conservation, high melting point metals and active metals are used as scrap or products generated in processes such as agglomeration and processing, and in recent years there has been a strong desire to recycle scrap that is not used due to end of life or unnecessary use. Recyclable scraps (hereinafter referred to as recycled raw materials) generated in the manufacturing process and usage of these metals and alloys are remelted in a high vacuum or in a low pressure vacuum purged with high purity inert gas. It is known to form agglomerates. These known melting and agglomeration methods include electron beam (high voltage) melting, vacuum arc (low voltage) melting, arc (low voltage) melting in an inert gas atmosphere, plasma melting, etc. as well as melting of purgin raw materials. means are mainly used. Typical examples of alloys of high melting point active metals are shown in Table 1.

【表】【table】

【表】 これらのうちで、ジルカロイ−2、Ti−6Al−
4Vなどの合金は、前者は原子力工業用に、また
后者は航空機工業を主体として広く機械構造材用
として、その利用が高まりつゝある。そのため生
産量および使用量の増加とともに、スクラツプ発
生量も多くなり、その再生が強く望まれている。 それら合金の再生原料の再溶解では、すでに仕
様値の範囲内に調整ずみの組成比から、変化の少
ない再溶解方法が強く望まれる。 例えば前述の2合金について添加元素の蒸気圧
を比較すると表−2の通りである。
[Table] Among these, Zircaloy-2, Ti-6Al-
The use of alloys such as 4V is increasing, with the former used for the nuclear power industry, and the latter used for a wide range of mechanical structural materials, mainly in the aircraft industry. Therefore, as the amount of production and usage increases, the amount of scrap generated also increases, and there is a strong desire to recycle it. When remelting recycled raw materials for these alloys, a remelting method that minimizes changes in the composition ratio, which has already been adjusted within the specification range, is strongly desired. For example, Table 2 shows a comparison of the vapor pressures of added elements for the two alloys mentioned above.

【表】 上記のジルカロイ−2では、該合金の融点にお
けるCrの蒸気圧はZrの蒸気圧の約105倍であり、
高温に加熱、保持するとCrの選択蒸発が盛んに
起ることは容易に理解しうるところである。 バージン原料の溶解では、それぞれの添加元素
の蒸発ロス(溶解后の歩留り)を見込んで、溶解
原料中へ添加元素を添加している。その溶解時の
歩留りは、例えばジルカロイ−2中でのCrにお
いては、 高電圧電子ビーム溶解 5〜40% 低電圧プラズマビーム溶解 40〜60% 消耗電極式アーク溶解 ≒90% であることが報告されている。 ルーズな形状をした再生原料の溶解方法として
は、上述の高電圧電子ビーム、もしくは低電圧プ
ラズマビームを加熱源とする溶解法が可能である
が、それらの方法で直接健全な合金インゴツトを
造塊する場合、前述のようにCrの歩留りが悪
く、そのためCr成分の調整と均一性の保持(仕
様値内におさまり、かつ偏析のないこと)は極め
て困難である。 プラズマ・ビーム溶解法では比較的歩留りはよ
いが、大型インゴツト造塊の場合、部分的に所望
の組成範囲外の組成部分を発生する場合があり、
一方、消耗電極式アーク(以下ARと略称する)
では、消耗電極の準備が必要である。そして消耗
電極としての必要条件は、 1 大電流の通過に十分なよう、棒状に接続(融
着)されていること 2 接続(融着)部が組成変化していないこと。
添加元素の減少が少い。また異物(TIG溶接に
おけるWのまき込み)、および活性有害ガス
(O2,N2,CO2など)による汚染のないこと。 などがあげられる。 従来、ジルカロイ−2,Ti−6Al−4Vなどに代
表される高融点金属および活性金属の合金の再生
原料の溶解に際して、添加元素の減少が少なく、
かつ汚染もしくは異物の混入がほとんどない造塊
プロセスは見当らなかつた。 本発明はこれら従来法を改良し、活性金属、高
融点金属及びこれら金属の合金の再生原料から所
望組成の粗インゴツトを造塊する方法であり、本
発明の要旨とするところは前記特許請求の範囲に
明記したとおりであり、更に具体的には、水冷銅
ハース(横断面が角型が好ましい)を備えた真空
プラズマ溶解炉で再生原料の表層部を溶解し、二
次溶解用の消耗電極をつくる。その場合、必要に
より添加元素を追加する場合もある。 再生原料は、溶解前に水冷銅ハース内にチヤー
ジし、また溶解炉に付属した原料投入系から追加
チヤージされる。その場合の溶解法としては十分
なとけ込みの必要はなく、前述のような消耗電極
として必要な条件を満たし得る程度に融着してお
れば良い。 このようにして得た溶解棒を用いて消耗電極式
アーク溶解を行つて所望の粗インゴツトを得る。
得られた粗インゴツトはバージン原料から造塊し
た粗インゴツトと全く同様に表面を切削仕上げし
て製品インゴツトとし、爾後の鍛造、圧延、押出
し等の加工工程に用いることができる。 以下に本発明方法をジルカロイ−2の再生原料
から粗インゴツトを造塊する実施例を説明する。 実施例 準備した再生原料の発生源にもとづく分類、形
状、重量および組成比を表−3に示す。 低電圧プラズマビーム炉の水冷銅ハースの形状
は、断面が140mm×140mm、長さが1M800mmであ
る。
[Table] In Zircaloy-2 mentioned above, the vapor pressure of Cr at the melting point of the alloy is approximately 10 5 times that of Zr,
It is easy to understand that selective evaporation of Cr occurs actively when heated and held at high temperatures. When melting virgin raw materials, additional elements are added to the melted raw materials taking into consideration the evaporation loss (yield after melting) of each additional element. It has been reported that the yield during melting of Cr in Zircaloy-2, for example, is 5-40% for high-voltage electron beam melting, 40-60% for low-voltage plasma beam melting, and ≒90% for consumable electrode arc melting. ing. As a method for melting recycled raw materials that have a loose shape, it is possible to use the above-mentioned melting method using a high-voltage electron beam or a low-voltage plasma beam as a heating source, but it is possible to directly form a healthy alloy ingot using these methods. In this case, as mentioned above, the yield of Cr is poor, and therefore it is extremely difficult to adjust the Cr content and maintain uniformity (within specification values and without segregation). Plasma beam melting has a relatively good yield, but in the case of large ingot agglomeration, compositions may be partially outside the desired composition range.
On the other hand, consumable electrode type arc (hereinafter abbreviated as AR)
Now we need to prepare the consumable electrodes. The necessary conditions for a consumable electrode are: 1. It must be connected (fused) in a rod shape to be able to pass a large current. 2. The composition of the connected (fused) part must not change.
Less reduction in added elements. Also, there shall be no contamination by foreign matter (W infusion during TIG welding) and active harmful gases (O 2 , N 2 , CO 2, etc.). etc. Conventionally, when melting recycled raw materials for alloys of high melting point metals and active metals such as Zircaloy-2, Ti-6Al-4V, etc., the amount of added elements decreases little.
Moreover, no agglomeration process with almost no contamination or foreign matter was found. The present invention improves these conventional methods and is a method for forming crude ingots of a desired composition from recycled raw materials of active metals, high melting point metals, and alloys of these metals. As specified in the scope, more specifically, the surface layer of the recycled raw material is melted in a vacuum plasma melting furnace equipped with a water-cooled copper hearth (preferably a rectangular cross section), and a consumable electrode for secondary melting is used. Create. In that case, additional elements may be added if necessary. The recycled raw material is charged into a water-cooled copper hearth before melting, and is additionally charged from the raw material input system attached to the melting furnace. In this case, the melting method does not require sufficient melting, and it is sufficient to fuse the material to an extent that satisfies the conditions necessary for a consumable electrode as described above. Using the melting rod thus obtained, consumable electrode type arc melting is performed to obtain a desired rough ingot.
The surface of the obtained rough ingot is cut and finished in exactly the same way as a rough ingot formed from virgin raw materials to obtain a product ingot, which can be used in subsequent processing steps such as forging, rolling, and extrusion. An example of the method of the present invention for forming crude ingots from recycled raw materials of Zircaloy-2 will be described below. Example Table 3 shows the classification, shape, weight, and composition ratio of the prepared recycled raw materials based on their source. The water-cooled copper hearth of the low-voltage plasma beam reactor has a cross section of 140mm x 140mm and a length of 1M800mm.

【表】 真空プラズマ溶解炉における溶解条件は電流
1.5KA,電圧65Vで溶解時の圧力は1×10-2トー
ルの範囲内である。(Arガスに置換されている) 溶解原料は全部の約60%に相当する鍛造材端
は、溶解前に水冷銅ハース内にチヤージされてお
り、残りの約40%のうちの管端、圧延板端の再生
原料は、長さをそれぞれ50mm以下に切断し、切削
片圧縮体とともに原料供給系にチヤージする。
Crについては約15%程度の蒸発ロスの補償のた
めZr−Cr合金ボタン(配合比(重量%)80Zr−
20Crで1ケの重量15g)20ケを添加元素供給系
にチヤージする。 プラズマビーム溶解は、まずハース内にチヤー
ジの原料(鍛造材端)の表層部を溶解し、その后
原料および添加元素(Zr−Cr合金ボタン)を追
加チヤージしてこれら材料の表層部を溶解する。
添加元素ボタンの本溶解でのチヤージは10個でハ
ース端90mmの位置から180mmの移動毎に1個投入
している。全再生原料は48分間で溶解された。 溶解後の重量は209.8Kgである。このプラズマ
ビーム溶解での重量ロスは0.095%の極めて少な
い値であつた。 溶解棒は、溶融部は全長にわたり、それぞれの
断面での12〜25%程度の範囲で、溶融部もその
まゝ溶湯に保持されて過熱されることなく、下部
の間隙部にとけ落ち、下部の未溶融塊の融着に役
立つ。 プラズマビーム溶解棒はその后300mm水冷銅モ
ールドを使用した消耗電極式アーク溶解炉で溶解
した、その諸条件を下記に示す。 インゴツト 重量 192.8Kg 寸法 直径296mm×長さ437mm 消耗電極とけ残り 重量 15.4Kg アーク電流 7.0KA アーク電圧 33V 溶解時の圧力 1〜3×10-3torr 得られたインゴツトの上、中、下各部について
中央部、周辺部から分析用試料を採取し、螢光X
線分析で成分比をもとめた。その結果を表4にそ
の値を示す。 またO2は原料の平均値が1170p.p.mであつたが
消耗電極式アーク溶解によるインゴツトの平均値
は1090p.p.mで本プロセス汚染が皆無であつてこ
とが示されている。
[Table] The melting conditions in a vacuum plasma melting furnace are current
The pressure during melting is within the range of 1×10 -2 Torr at 1.5KA and 65V voltage. (Substituted with Ar gas) The end of the forged material, which accounts for about 60% of the total melted raw material, is charged in a water-cooled copper hearth before melting, and the remaining 40% is the pipe end, rolled The recycled raw material at the end of the plate is cut into pieces of 50 mm or less in length and charged to the raw material supply system together with the compressed cut pieces.
Regarding Cr, in order to compensate for the evaporation loss of about 15%, Zr-Cr alloy button (mixing ratio (weight%) 80Zr-
Charge 20 pieces of 20Cr (one piece weighs 15g) to the additive element supply system. Plasma beam melting first melts the surface layer of the charged raw material (end of the forged material) in the hearth, and then additionally charges the raw material and additive elements (Zr-Cr alloy button) to melt the surface layer of these materials. .
The charge for the main melting of the additive element buttons is 10, and one button is charged every 180 mm from the hearth end position of 90 mm. All recycled material was dissolved in 48 minutes. The weight after dissolution is 209.8Kg. The weight loss in this plasma beam melting was an extremely small value of 0.095%. The molten rod has a molten part that spans the entire length and ranges from 12 to 25% of each cross section, and the molten part is retained in the molten metal without being overheated and melts into the gap at the bottom. Useful for fusing unmelted lumps. The plasma beam melted rod was then melted in a consumable electrode type arc melting furnace using a 300 mm water-cooled copper mold.The conditions are shown below. Ingot Weight 192.8Kg Dimensions Diameter 296mm x Length 437mm Consumable electrode unmelted Weight 15.4Kg Arc current 7.0KA Arc voltage 33V Pressure during melting 1 to 3 x 10 -3 torr The center of the top, middle and bottom of the obtained ingot Collect a sample for analysis from the surrounding area, and
The component ratio was determined by line analysis. The results are shown in Table 4. Furthermore, the average value of O 2 for the raw material was 1170 p.pm, but the average value for the ingot produced by consumable electrode arc melting was 1090 p.pm, indicating that there was no contamination in this process.

【表】 本発明方法により再生原料から消耗電極式アー
ク溶解による粗インゴツト(プラズマビーム溶解
及び消耗電極式アーク溶解)の添加元素の歩留り
は表−5に示す通りである。
[Table] Table 5 shows the yield of added elements in crude ingots produced by consumable electrode arc melting (plasma beam melting and consumable electrode arc melting) from recycled raw materials according to the method of the present invention.

【表】 量の補正あり
表−5中特に蒸気圧が高く蒸発し易いCrにつ
いて従来法と比較すると、Crの歩留りが前述し
た如く高電圧電子ビーム溶解では0.05〜0.4、低
電圧プラズマビーム溶解で0.4〜0.6に比し、格段
に秀れた歩留りを示し、かつインゴツト各部に亙
つて均質であることが認められた。 Cr以外の添加元素Sn,Fe,Niはそれぞれ95%
以上の歩留りを示し、従つて本発明では成分比の
調整が極めて実施し易いことが明らかである。 以上ジルカロイ−2の実施例について詳述した
が活性金属及び高融点金属、更にTi−6Al−4V合
金、Ta合金、Nb合金等、これら金属の合金につ
いても同様に適用できるものであり、単一金属
(純金属)においては消耗電極を作成する場合に
汚染をうけることがなくかつ蒸発ロスが極めて少
ない等の利点がある。
[Table] Amount correction is included. In Table 5, when comparing Cr with the conventional method, which has a high vapor pressure and is easy to evaporate, the yield of Cr is 0.05 to 0.4 in high-voltage electron beam melting, and 0.4 to 0.4 in low-voltage plasma beam melting, as mentioned above. It was found that the yield was much better than that of 0.4 to 0.6, and that the ingot was homogeneous in all parts. Additive elements other than Cr: Sn, Fe, and Ni are each 95%
The above yield is shown, and it is therefore clear that adjustment of the component ratio is extremely easy to implement in the present invention. Although the example of Zircaloy-2 has been described in detail above, it can be similarly applied to active metals, high melting point metals, and alloys of these metals such as Ti-6Al-4V alloy, Ta alloy, Nb alloy, etc. Metals (pure metals) have advantages such as being free from contamination when making consumable electrodes and having extremely low evaporation loss.

Claims (1)

【特許請求の範囲】 1 チタン、ジルコニウムなどの活性金属又はタ
ンタル、ニオブ、モリブデン、タングステン等の
高融点金属或はこれら金属を基体とする合金の再
生原料と、水冷銅ハースを有する真空プラズマ溶
解炉内で該再生原料の表層部を溶解して棒状に造
塊する工程とこの棒状体を消耗電極として真空ア
ーク溶解する工程との結合からなる活性金属又は
高融点金属或はこれら金属の合金の粗インゴツト
を造塊する方法。 2 前記造塊工程における再生原料の表層部溶解
が該原料断面の約12〜25%である特許請求の範囲
第1項記載の粗インゴツトを造塊する方法。 3 前記金属を基体とする合金の粗インゴツトを
製造するに当り、真空プラズマ溶解工程で成分調
整を行う特許請求の範囲第1項記載の粗インゴツ
トを造塊する方法。
[Claims] 1. A vacuum plasma melting furnace having a recycled raw material of active metals such as titanium and zirconium, high melting point metals such as tantalum, niobium, molybdenum, and tungsten, or alloys based on these metals, and a water-cooled copper hearth. A method for producing active metals, high-melting point metals, or alloys of these metals, which consists of a process of melting the surface layer of the recycled raw material to form a rod-like agglomerate, and a process of vacuum arc melting using this rod-like body as a consumable electrode. A method of making ingots. 2. The method for agglomerating a crude ingot according to claim 1, wherein the surface layer portion of the recycled raw material in the agglomeration step is dissolved to about 12 to 25% of the cross section of the raw material. 3. The method for forming a coarse ingot according to claim 1, wherein the composition is adjusted in a vacuum plasma melting step in producing the coarse ingot of the alloy based on the metal.
JP5702479A 1979-05-11 1979-05-11 Molding method for crude ingot of active metal or high- melting-point metal or alloy of these metals Granted JPS55149770A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5702479A JPS55149770A (en) 1979-05-11 1979-05-11 Molding method for crude ingot of active metal or high- melting-point metal or alloy of these metals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5702479A JPS55149770A (en) 1979-05-11 1979-05-11 Molding method for crude ingot of active metal or high- melting-point metal or alloy of these metals

Publications (2)

Publication Number Publication Date
JPS55149770A JPS55149770A (en) 1980-11-21
JPS6115786B2 true JPS6115786B2 (en) 1986-04-25

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62282686A (en) * 1986-06-02 1987-12-08 Iwasaki Electric Co Ltd Water treatment device

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JPS57155332A (en) * 1981-03-18 1982-09-25 Shinku Yakin Kk Method for regenerating metallic electrode base material and casting crude ingot of titanium or titanium base alloy
JPS6473028A (en) * 1987-09-16 1989-03-17 Tosoh Corp Recovering method for high purity tantalum from scrap tantalum
JPS6475632A (en) * 1987-09-18 1989-03-22 Tosoh Corp Recovering method for tantalum from scrap tantalum
AT399513B (en) * 1990-10-05 1995-05-26 Boehler Edelstahl METHOD AND DEVICE FOR PRODUCING METALLIC ALLOYS FOR PRE-MATERIALS, COMPONENTS, WORKPIECES OR THE LIKE OF TITANIUM-ALUMINUM BASE ALLOYS
CN104611720A (en) * 2015-01-28 2015-05-13 江苏理工学院 A method for producing electrolytic nickel and recovering tin and iron from tin-nickel-iron alloy waste
CN111676380B (en) * 2018-05-25 2021-06-25 南京尚吉增材制造研究院有限公司 Short-process preparation device for titanium and titanium alloy
CN111593207B (en) * 2020-04-17 2021-09-14 陕西斯瑞新材料股份有限公司 Preparation method of low-cost fine-grain CuCr contact material

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5326205B2 (en) * 1973-04-11 1978-08-01
JPS5162139A (en) * 1974-11-28 1976-05-29 Daido Steel Co Ltd Moribuden oyobi moribudengokinchukaino seizoho

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62282686A (en) * 1986-06-02 1987-12-08 Iwasaki Electric Co Ltd Water treatment device

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