JP3178297B2 - Method for transferring Cu or Cu alloy - Google Patents

Method for transferring Cu or Cu alloy

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Publication number
JP3178297B2
JP3178297B2 JP07786295A JP7786295A JP3178297B2 JP 3178297 B2 JP3178297 B2 JP 3178297B2 JP 07786295 A JP07786295 A JP 07786295A JP 7786295 A JP7786295 A JP 7786295A JP 3178297 B2 JP3178297 B2 JP 3178297B2
Authority
JP
Japan
Prior art keywords
molten metal
inert gas
concentration
alloy
cover member
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 - Lifetime
Application number
JP07786295A
Other languages
Japanese (ja)
Other versions
JPH08276260A (en
Inventor
一孝 國井
研治 大隅
清正 大賀
基浩 新井
裕文 岡田
栄次 吉田
穣司 益田
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel Ltd
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Filing date
Publication date
Application filed by Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP07786295A priority Critical patent/JP3178297B2/en
Publication of JPH08276260A publication Critical patent/JPH08276260A/en
Application granted granted Critical
Publication of JP3178297B2 publication Critical patent/JP3178297B2/en
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Expired - Lifetime legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)
  • Continuous Casting (AREA)

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、溶解工程で脱酸処理し
て酸素(O2 )濃度を10ppm以下にしたCuまたは
Cu合金の溶湯を、鋳造工程に移湯する方法に関するも
のであり、特に移湯時における溶湯中のO2 濃度が増加
することを防止する様にしたCuまたはCu合金の移湯
方法に関するものである。
The present invention relates to oxygen (O 2) and deacidification with lysis step a melt of Cu or Cu alloy has a concentration of 10ppm or less, relates to a method of Utsuriyu the casting process, In particular, the present invention relates to a method for transferring Cu or Cu alloy in which the O 2 concentration in the molten metal is prevented from increasing at the time of transferring the molten metal.

【0002】[0002]

【従来の技術】CuおよびCu合金(以下、Cu合金で
代表することがある)は、電気および熱の良導体である
と共に、加工性にも優れているので、電気、電子および
熱交換等の分野で幅広く利用されている。ところでCu
合金製品の特性は、Cu合金中のO2 濃度に影響され、
一般的にO2 濃度の低減が製品々質の向上につながり、
Cu合金中のO2 濃度はできるだけ低い方が好ましいと
されている。こうしたことから、Cu合金の溶解・鋳造
工程においては、各種の溶湯脱酸法や脱酸した溶湯の再
度酸化防止策が従来から実施されている。
2. Description of the Related Art Cu and Cu alloys (hereinafter sometimes referred to as Cu alloys) are good conductors of electricity and heat and are also excellent in workability. Widely used in By the way, Cu
The properties of the alloy products are affected by the O 2 concentration in the Cu alloy,
In general, reduction of O 2 concentration leads to improvement of product quality,
It is considered that the O 2 concentration in the Cu alloy is preferably as low as possible. For this reason, in the melting and casting process of the Cu alloy, various molten metal deoxidation methods and measures to prevent reoxidation of the deoxidized molten metal have been conventionally performed.

【0003】溶湯脱酸法としては、ポーリングと呼ばれ
る方法が古くから知られている。この方法は、溶湯中に
生松丸太を投入して、生木から出るCOやH2 等のガス
によって、溶湯中のCu2 Oを還元するものである。ま
た本発明者らは、特開平5−25559号の様な溶湯脱
酸法も提案している。この技術は、Cu合金溶湯の溶湯
表面に木炭等の固体還元剤を散布した後、Arガス等の
不活性ガスをCu合金溶湯中に吹き込み、および/また
は、不活性ガスをCu合金溶湯表面に吹く付けるもので
あり、こうした構成を採用することによって、発生する
CO2 ガスを溶湯中および溶湯表面から可及的速やかに
除去することを可能にしたものである。一方、脱酸した
溶湯の再度酸化防止策としては、通常溶湯表面をカーボ
ン系固体還元剤で覆ったり、溶湯表面の周囲雰囲気をC
Oガス等の還元性ガス雰囲気とする方法が行われてい
る。これらの溶湯脱酸法および再酸化防止策によって、
一応の効果が得られている。
As a molten metal deoxidation method, a method called poling has been known for a long time. In this method, raw pine logs are put into the molten metal, and Cu 2 O in the molten metal is reduced by a gas such as CO or H 2 emitted from the raw wood. The present inventors have also proposed a molten metal deoxidation method as disclosed in JP-A-5-25559. In this technique, after a solid reducing agent such as charcoal is sprayed on the surface of the molten Cu alloy, an inert gas such as Ar gas is blown into the molten Cu alloy and / or an inert gas is sprayed on the surface of the molten Cu alloy. This configuration makes it possible to remove generated CO 2 gas in the molten metal and from the surface of the molten metal as quickly as possible. On the other hand, as measures to prevent the deoxidized molten metal from re-oxidizing, the surface of the molten metal is usually covered with a carbon-based solid reducing agent,
A method of using a reducing gas atmosphere such as O gas has been used. With these molten metal deoxidation methods and reoxidation prevention measures,
A certain effect has been obtained.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、現実問
題として、最終的に得られる鋳塊は、希望するよりも多
量のO2 を含んでいるのが実情である。即ち、溶解炉で
脱酸処理してO2 濃度が10ppm以下のJIS無酸素
銅レベルの溶湯が得られても、通常の工程に従って鋳造
すると、得られた鋳塊中のO2 濃度は少なくとも15〜
20ppm程度になるのが一般的であり、溶解炉で得ら
れたO2 濃度レベルを鋳塊中にそのまま維持することは
極めて困難であった。これは、溶解炉で脱酸処理された
溶湯を鋳造機に移湯する際に、何らかの原因で溶湯中に
混入するものと考えられる。
However, as a practical matter, the fact is that the ingot finally obtained contains a larger amount of O 2 than desired. That is, even if the O 2 concentration is treated deoxidation obtained following JIS oxygen-free copper levels of the molten metal 10ppm in a melting furnace and cast according to conventional processes, the O 2 concentration in the obtained ingot is at least 15 ~
It is generally about 20 ppm, and it is extremely difficult to maintain the O 2 concentration level obtained in the melting furnace in the ingot as it is. This is thought to be due to mixing in the molten metal for some reason when the molten metal deoxidized in the melting furnace is transferred to the casting machine.

【0005】こうしたことから、極めて良好な特性を発
揮することのできる無酸素銅レベルの鋳塊を製造するに
は、真空溶解法や真空鋳造法を実施したり、専用の溶解
設備を用いたりしているが、生産性の面で或はコスト的
に問題がある。
[0005] Therefore, in order to produce an oxygen-free copper level ingot capable of exhibiting extremely good properties, a vacuum melting method or a vacuum casting method is used, or a special melting facility is used. However, there is a problem in terms of productivity or cost.

【0006】本発明はこうした従来技術における技術的
課題を解決する為になされたものであって、その目的
は、移湯時における溶湯中のO2 濃度が増加することを
防止し、一般的な溶解・鋳造設備であっても、無酸素銅
レベルの鋳塊を製造することのできるCuまたはCu合
金の移湯方法を提供することにある。
The present invention has been made to solve such technical problems in the prior art, and an object of the present invention is to prevent the O 2 concentration in the molten metal from increasing at the time of hot water transfer, and It is an object of the present invention to provide a method for transferring Cu or a Cu alloy capable of producing an ingot of oxygen-free copper level even in a melting and casting facility.

【0007】[0007]

【課題を解決するための手段】上記目的を達成した本発
明とは、溶解工程における脱酸処理によって、酸素濃度
を10ppm以下にしたCuまたはCu合金の溶湯を、
鋳造工程に移湯するに際して、溶解炉から鋳造機までの
移湯過程中に存在する溶湯落差部のうち、少なくとも落
下高さが20mm以上の溶湯落差部をカバー部材で覆
い、この覆われた領域に不活性ガス気流を形成する点に
要旨を有するCuまたはCu合金の移湯方法である。
According to the present invention, which has achieved the above object, there is provided a method for producing a molten copper or Cu alloy having an oxygen concentration of 10 ppm or less by a deoxidizing treatment in a melting step.
When the molten metal is transferred to the casting step, at least the molten metal drop portion having a drop height of 20 mm or more is covered with a cover member among the molten metal drop portions existing during the process of transferring the molten metal from the melting furnace to the casting machine. This is a method for transferring Cu or a Cu alloy having a gist in forming an inert gas flow.

【0008】上記方法において、前記カバー部材に不活
性ガス導入孔および不活性ガス排出孔を設け、前記不活
性ガス導入孔から前記領域の容積の0.2倍/分以上の
流量で不活性ガスを導入すると共に、前記不活性ガス排
出孔から排出する構成を採用することが有効であり、こ
れによって本発明の効果が最大限に発揮される。
In the above method, an inert gas introduction hole and an inert gas discharge hole are provided in the cover member, and the inert gas is introduced from the inert gas introduction hole at a flow rate of 0.2 times / min or more of the volume of the region. It is effective to adopt a configuration in which the inert gas is introduced from the inert gas discharge hole while introducing the gas, so that the effect of the present invention is maximized.

【0009】[0009]

【作用】本発明者らは、溶解炉から鋳造機に移湯する際
に、Cu合金(またはCu)溶湯中のO2 濃度が増加す
る原因について、様々な角度から検討した。その結果、
溶解炉から鋳造機までの移湯過程中に存在する溶湯落差
部が、O2 濃度の増加に大きく影響することが判明し
た。即ち、移湯過程においては、図1に示す様に、溶解
炉1と移湯樋2の間、移湯樋2の相互間、移湯樋2と鋳
造樋3の間、更には鋳造樋3と鋳造機4の間には、溶湯
落差部5が存在し、この溶湯落差部5はその構造上解消
することはできないのであるが、この溶湯落差部5が移
湯時の溶湯6中のO2 濃度の増加に大きく影響すること
が判明した。その理由はおそらく、上記溶湯落差部5に
おいては、溶湯6はあたかも滝の如く流れ、溶湯6の表
面積が急激に増加すること、および溶湯落差部5では固
体還元剤等で被覆することが困難であり、移湯過程中は
外気に露出した状態であること等によって、この部分で
溶湯6が外気中のO2 を吸収するものと考えられる。
The present inventors have studied from various angles the cause of an increase in the O 2 concentration in a molten Cu alloy (or Cu) when a molten metal is transferred from a melting furnace to a casting machine. as a result,
It has been found that the molten metal drop existing during the molten metal transfer process from the melting furnace to the casting machine has a great effect on the increase in the O 2 concentration. That is, in the hot water transfer process, as shown in FIG. Between the casting machine 4 and the casting machine 4, there is a molten metal head 5 which cannot be eliminated due to its structure. (2 ) It was found that it greatly affected the increase in concentration. This is probably because the molten metal 6 flows as if it were a waterfall in the molten metal head 5, and the surface area of the molten metal 6 increases rapidly, and it is difficult to coat the molten metal head 5 with a solid reducing agent or the like. It is considered that the molten metal 6 absorbs O 2 in the outside air at this portion because the molten metal 6 is exposed to the outside air during the hot water transfer process.

【0010】そこで本発明者らは、上記溶湯落差部5に
おけるO2 の吸収を防止するという観点から、更に検討
した。その結果、上記溶湯落差部5のうち少なくとも所
定の落下高さを有する溶湯落差部5を、後記カバー部材
によって覆い、該覆われた領域に不活性気流を形成すれ
ば、溶湯6へのO2 の吸収が防止され、溶解炉において
低減されたO2 濃度が移湯過程において増加することな
く、該O2 濃度を維持したまま鋳塊が製造できることを
見いだし、本発明を完成した。
The present inventors have further studied from the viewpoint of preventing the absorption of O 2 in the molten metal drop section 5. As a result, if the molten metal head 5 having at least a predetermined falling height among the molten metal heads 5 is covered with a cover member described below and an inert gas flow is formed in the covered area, O 2 to the molten metal 6 can be formed. the absorption is prevented, reduced O 2 concentrations in melting furnace without increasing the Utsuriyu process, mass cast while maintaining the O 2 concentration is found that can be produced, and have completed the present invention.

【0011】本発明者らが、溶湯落差部5が外気に露出
した状態で、溶湯落差部5の高さと溶湯6のO2 濃度増
加量との関係について調査したところ、図2に示す結果
が得られた。尚このときの溶解・移湯条件は下記の通り
である。 (溶解・移湯条件) 溶湯品種 :純Cu(溶湯中の初期O2 濃度:10ppm) 溶湯温度 :1200℃ 移湯樋2の幅:500mm 溶湯深さ :300mm 溶湯流速 :40kg/分
The inventors of the present invention have investigated the relationship between the height of the molten metal head 5 and the increase in the O 2 concentration of the molten metal 6 with the molten metal head 5 exposed to the outside air. The results shown in FIG. Obtained. The conditions for dissolution and hot water transfer are as follows. (Melting / migration conditions) Melt type: Pure Cu (Initial O 2 concentration in the melt: 10 ppm) Melt temperature: 1200 ° C. Width of the gutter 2: 500 mm Melt depth: 300 mm Melt flow rate: 40 kg / min

【0012】図2から明らかな様に、溶湯落差部5の高
さが20mm以上になると、溶湯6中のO2 濃度は10
ppm以上も増加し(即ち、溶湯中のO2 濃度は20p
pm以上になる)、O2 濃度が10ppm以下の無酸素
銅レベルのものを得るという初期の目的は達成されなく
なる。本発明は、後記実施例に示す様に、この様な状況
のもとにおいても、移湯過程中でのO2 の吸収を防止
し、溶湯中のO2 濃度を10ppmに維持できたのであ
る。即ち、本発明は、少なくとも落下高さが20mm以
上になる溶湯落差部5において実施する必要がある。
As is apparent from FIG. 2, when the height of the molten metal drop 5 becomes 20 mm or more, the O 2 concentration in the molten metal 6 becomes 10%.
ppm (that is, the O 2 concentration in
pm or more) and the initial goal of obtaining oxygen-free copper levels with O 2 concentrations of 10 ppm or less is no longer achieved. According to the present invention, as shown in the examples described below, even under such a situation, it was possible to prevent the absorption of O 2 during the process of hot water transfer and maintain the O 2 concentration in the molten metal at 10 ppm. . That is, the present invention needs to be implemented at least in the molten metal drop portion 5 where the drop height is 20 mm or more.

【0013】本発明は上記の如く、溶湯落差部5をカバ
ー部材7によって覆うと共に、該覆われた領域に不活性
気流を形成する点に特徴を有するものであるが、本発明
者らはその具体的構成についても検討した。その結
果、、例えば溶解炉1と移湯樋2の間については図3
に、移湯樋2の相互間については図4に夫々示す様に、
溶湯落差部5の周囲をカバー部材7で覆うと共に、該カ
バー部材7によって覆われた領域8に不活性ガス導入孔
9および不活性ガス排出孔10を設けておき、前記不活
性ガス導入孔9からAr等の不活性ガスを導入すると共
に、前記不活性ガス排出孔10から当該ガスを排出して
前記領域8内に不活性気流を形成する構成が特に有効で
あることがわかった。尚図3において、11は溶湯6の
表面上に散布された固体還元剤を示し、また溶解炉1は
出湯時に矢印Aの方向に傾動されるものである。
As described above, the present invention is characterized in that the molten metal head 5 is covered with the cover member 7 and an inert gas flow is formed in the covered area. The specific configuration was also discussed. As a result, for example, between the melting furnace 1 and the hot water gutter 2, FIG.
In addition, as shown in FIG.
The periphery of the molten metal drop portion 5 is covered with a cover member 7, and an inert gas introduction hole 9 and an inert gas discharge hole 10 are provided in a region 8 covered by the cover member 7. It has been found that a configuration in which an inert gas such as Ar is introduced from above and the gas is discharged from the inert gas discharge hole 10 to form an inert gas flow in the region 8 is particularly effective. In FIG. 3, reference numeral 11 denotes a solid reducing agent sprayed on the surface of the molten metal 6, and the melting furnace 1 is tilted in the direction of arrow A when the molten metal is poured.

【0014】このとき用いる不活性ガスは、前記領域8
の容積の0.2倍/分以上の流量で導入するのが好まし
い。即ち、図5は、不活性ガスの流量(前記領域8の容
積に対する割合:倍/分)と溶湯6中のO2 増加量の関
係を示すグラフであるが、その流量が0.2倍/分以上
のときに溶湯6中のO2 増加量が極めて抑制されている
ことが分かる。尚このときの条件は、不活性ガスとして
Ar(Arガス圧:5kg/cm2 )を用いる以外は、
前記図2のときを同じとした。この様に不活性ガスの流
量によって溶湯6中のO2 増加量が変化するのは、前記
カバー部材7によって溶湯落差部5を外気からいかに遮
断しても、僅かな空隙を通ってくる空気、或は溶湯6の
表面に随伴してくる空気等が、溶湯落差部5における攪
拌効果によって溶湯6中に吸収されるものと考えられ
る。従って、不活性ガスの流量を上記の様に設定するこ
とは、上記のような状況のもとでも、不活性ガス雰囲気
を確保して溶湯6中へのO2 の吸収を防止する上で極め
て有意義である。
The inert gas used at this time is in the region 8
It is preferable to introduce at a flow rate of 0.2 times / min or more of the volume. That is, FIG. 5 is a graph showing the relationship between the flow rate of the inert gas (the ratio to the volume of the region 8: times / minute) and the amount of increase in O 2 in the molten metal 6. It can be seen that the amount of increase in O 2 in the molten metal 6 is extremely suppressed when the time is equal to or longer than minutes. The conditions at this time were as follows, except that Ar (Ar gas pressure: 5 kg / cm 2 ) was used as the inert gas.
The case of FIG. 2 was the same. As described above, the amount of increase in O 2 in the molten metal 6 varies depending on the flow rate of the inert gas because no matter how the molten metal head 5 is cut off from the outside air by the cover member 7, air passing through a small gap, Alternatively, it is considered that air or the like accompanying the surface of the molten metal 6 is absorbed into the molten metal 6 by the stirring effect in the molten metal head 5. Therefore, setting the flow rate of the inert gas as described above is extremely important in securing the inert gas atmosphere and preventing the absorption of O 2 into the molten metal 6 even under the above-described circumstances. It is significant.

【0015】本発明で用いるカバー部材7の材質につい
ては、溶湯落差部5の周囲を覆うことができ且つ耐熱性
であれば特に限定されるものではなく、各種の金属材料
や耐火物が挙げられる。また用いる不活性ガスについて
も限定されるものではなく、前記したまた後記実施例に
示したArガスの他、窒素,ヘリウム等も用いることが
できる。
The material of the cover member 7 used in the present invention is not particularly limited as long as it can cover the periphery of the molten metal drop portion 5 and has heat resistance, and includes various metal materials and refractories. . The inert gas to be used is not limited, and nitrogen, helium, or the like can be used in addition to the Ar gas described above and in the following examples.

【0016】本発明では、移湯過程中に存在する溶湯落
差部5をカバー部材7によって覆うものであり、その効
果は前記の如く少なくとも落下高さが20mm以上の溶
湯落差部5に適用したときに発揮されるものである。従
って、後記実施例にも示す通り、カバー部材7によって
覆う溶湯落差部5を、その落下高さが20mm以上のと
ころだけを選択しても本発明の効果が達成される。しか
しながら、全ての溶湯落差部5(その落下高さが20m
m未満のところも含め)をカバー部材7によって覆い、
その領域8を外気から遮断する様にしても良いのは勿論
である。
In the present invention, the molten metal head 5 existing during the hot water transfer process is covered by the cover member 7, and the effect is obtained when the molten metal head 5 is applied to the molten metal head 5 having a drop height of at least 20 mm as described above. It is exhibited in. Therefore, as will be described later, the effect of the present invention can be achieved even if the molten metal dropping portion 5 covered by the cover member 7 is selected only at a position where the drop height is 20 mm or more. However, all the molten metal heads 5 (the height of which falls 20 m
m) is covered with the cover member 7,
Of course, the area 8 may be shielded from the outside air.

【0017】以下本発明を実施例によって更に詳細に説
明するが、下記実施例は本発明を限定する性質のもので
はなく、前・後記の趣旨に徴して設計変更することはい
ずれも本発明の技術的範囲に含まれるものである。
Hereinafter, the present invention will be described in more detail with reference to Examples. However, the following Examples are not intended to limit the present invention. It is included in the technical scope.

【0018】[0018]

【実施例】【Example】

実施例1 純CuおよびCu合金(Cu−Fe系)を、下記の条件
で溶解して脱酸処理したところ、O2 濃度が7ppmの
溶湯が得られた。 (溶解条件) 溶解炉 :高周波誘導炉(5t) 溶解温度 :1200℃ 脱酸処理 :木炭カバー+Arガス吹き込み(20Nl/分)
Example 1 Pure Cu and a Cu alloy (Cu-Fe system) were melted and deoxidized under the following conditions, and a molten metal having an O 2 concentration of 7 ppm was obtained. (Melting condition) Melting furnace: High frequency induction furnace (5t) Melting temperature: 1200 ° C Deoxidizing treatment: Charcoal cover + Ar gas injection (20Nl / min)

【0019】得られた溶湯を、溶解炉(出湯口直径:1
50mm)から落下高さ50mmの溶湯落差部5を通し
て、流速:50kg/分で移湯樋2に移湯した。このと
き、前記溶湯落差部5は、前記図3に示した様に、カバ
ー部材7によって覆った。尚遮断された領域8の容積
は、1m3 であり、この領域8内に流量:0.2m3
Arガスを導入して領域8内に気流を形成した。移湯樋
2に移湯した後の溶湯6中のO2 濃度を測定したとこ
ろ、7〜8ppmであり、殆ど増加していなかった。
The obtained melt is placed in a melting furnace (outlet diameter: 1).
(50 mm) through the molten metal head 5 having a drop height of 50 mm, and the molten metal was transferred to the hot water gutter 2 at a flow rate of 50 kg / min. At this time, the molten metal head 5 was covered with a cover member 7 as shown in FIG. The volume of the blocked area 8 was 1 m 3 , and an air flow was formed in the area 8 by introducing Ar gas at a flow rate of 0.2 m 3 into the area 8. When the O 2 concentration in the molten metal 6 after being transferred to the transfer trough 2 was measured, it was 7 to 8 ppm, and hardly increased.

【0020】上記溶湯6をその後鋳造機4まで移湯し、
鋳造を行った。このときの溶湯6は、その表面を黒鉛粉
(固体還元剤)で被覆した状態とした。鋳造機4に移湯
した後、50mm/分引き抜きの半連続鋳造によって溶
湯6を鋳造し(300mmφ×5本取り)、得られた鋳
塊のO2 濃度を測定したところ、7〜8ppmのままで
あった。
The molten metal 6 is then transferred to the casting machine 4,
Casting was performed. The surface of the molten metal 6 at this time was covered with graphite powder (solid reducing agent). After the molten metal was transferred to the casting machine 4, the molten metal 6 was cast by semi-continuous casting of 50 mm / min (300 mmφ × 5 pieces), and the O 2 concentration of the obtained ingot was measured. Met.

【0021】実施例2 純CuおよびCu合金(Cu−Ni系)を、下記の条件
で溶解して脱酸処理したところ、O2 濃度が10ppm
の溶湯が得られた。 (溶解条件) 溶解炉 :シャフト炉(5t/hr) 溶解温度 :1200℃ 脱酸処理 :シャフト炉の燃焼調整+原料調整
[0021] Example 2 pure Cu and Cu alloys (Cu-Ni-based), was dissolved and treated deoxidation under the following conditions, O 2 concentration is 10ppm
Was obtained. (Melting conditions) Melting furnace: Shaft furnace (5 t / hr) Melting temperature: 1200 ° C Deoxidation treatment: Combustion adjustment of shaft furnace + material adjustment

【0022】得られた溶湯6を、シャフト炉から出湯し
て移湯樋2(幅:300mm,深さ:200mm)に移
湯し、更にこの移湯樋2から落下高さ20mmの溶湯落
差部5を通して、流速:40kg/分で鋳造樋3に移湯
した。このとき、前記溶湯落差部5は、前記図4に示し
た様に、カバー部材7によって覆った。尚遮断された領
域8の容積は、0.5m3 であり、この領域8内に流
量:0.1m3 でArガスを導入して領域8内に気流を
形成した。また溶湯6は、シャフト炉から出湯した時点
から、鋳造機4に至るまで、その表面を黒鉛(固体還元
剤)で被覆した状態とした。移湯樋2上の溶湯6中のO
2 濃度を測定したところ、10ppmであり、殆ど増加
していなかった。
The obtained molten metal 6 is discharged from a shaft furnace and transferred to a hot water trough 2 (width: 300 mm, depth: 200 mm). 5 and flowed to the casting gutter 3 at a flow rate of 40 kg / min. At this time, the molten metal drop portion 5 was covered with a cover member 7 as shown in FIG. The volume of the blocked area 8 was 0.5 m 3 , and an Ar gas was introduced into the area 8 at a flow rate of 0.1 m 3 to form an air flow in the area 8. Further, the surface of the molten metal 6 was covered with graphite (solid reducing agent) from the time when the molten metal was discharged from the shaft furnace to the time when the molten metal 6 reached the casting machine 4. O in molten metal 6 on hot water gutter 2
2 When the concentration was measured, it was 10 ppm, and there was almost no increase.

【0023】上記溶湯6をその後鋳造機4に移湯した
後、30mm/分引き抜きの半連続鋳造によって溶湯6
を鋳造し(300mm□×2本取り)、得られた鋳塊の
2 濃度を測定したところ、10ppmのままであっ
た。
After the molten metal 6 is transferred to the casting machine 4, the molten metal 6 is subjected to semi-continuous casting of 30 mm / min.
Was cast (300 mm square x 2 pieces), and the O 2 concentration of the obtained ingot was measured.

【0024】[0024]

【発明の効果】以上述べた如く本発明法によれば、移湯
時における溶湯中の酸素濃度が増加することを防止する
ことができ、一般的な溶解・鋳造設備であっても、無酸
素銅レベルの鋳塊を製造することができる様になった。
As described above, according to the method of the present invention, it is possible to prevent the oxygen concentration in the molten metal from increasing at the time of hot water transfer, and even in a general melting / casting facility, It has become possible to produce copper level ingots.

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

【図1】一般的な溶湯移湯過程を説明する為の概略図で
ある。
FIG. 1 is a schematic view for explaining a general molten metal transfer process.

【図2】溶湯落差部5の高さと溶湯のO2 濃度増加量と
の関係を示すグラフである。
FIG. 2 is a graph showing the relationship between the height of a molten metal drop 5 and the increase in the O 2 concentration of the molten metal.

【図3】溶解炉1と移湯樋2の間の溶湯落差部5をカバ
ー部材7で覆った状態を示す概略説明図である。
FIG. 3 is a schematic explanatory view showing a state where a molten metal drop portion 5 between a melting furnace 1 and a hot water gutter 2 is covered with a cover member 7;

【図4】移湯樋2の相互間の溶湯落差部5をカバー部材
7で覆った状態を示す概略説明図である。
FIG. 4 is a schematic explanatory view showing a state where a molten metal drop portion 5 between the hot water transfer gutters 2 is covered with a cover member 7;

【図5】不活性ガスの流量と溶湯中のO2 増加量の関係
を示すグラフである。
FIG. 5 is a graph showing a relationship between a flow rate of an inert gas and an increase amount of O 2 in a molten metal.

【符号の説明】[Explanation of symbols]

1 溶解炉 2 移湯樋 3 鋳造樋 4 鋳造機 5 溶湯落差部 6 溶湯 7 カバー部材 8 領域 9 不活性ガス導入孔 10 不活性ガス排出孔 11 固体還元剤 DESCRIPTION OF SYMBOLS 1 Melting furnace 2 Transfer gutter 3 Casting gutter 4 Casting machine 5 Molten head 6 Molten 7 Cover member 8 Area 9 Inert gas introduction hole 10 Inert gas discharge hole 11 Solid reducing agent

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大賀 清正 兵庫県神戸市西区高塚台1丁目5番5号 株式会社神戸製鋼所 神戸総合技術研 究所内 (72)発明者 新井 基浩 兵庫県神戸市西区高塚台1丁目5番5号 株式会社神戸製鋼所 神戸総合技術研 究所内 (72)発明者 岡田 裕文 山口県下関市長府港町14番1号 株式会 社神戸製鋼所長府製造所内 (72)発明者 吉田 栄次 山口県下関市長府港町14番1号 株式会 社神戸製鋼所長府製造所内 (72)発明者 益田 穣司 山口県下関市長府港町14番1号 株式会 社神戸製鋼所長府製造所内 (56)参考文献 特開 昭53−80331(JP,A) 特開 平5−25559(JP,A) 実開 昭60−180998(JP,U) 実開 昭59−34839(JP,U) (58)調査した分野(Int.Cl.7,DB名) B22D 35/00 B22D 11/00 ──────────────────────────────────────────────────の Continuing on the front page (72) Inventor Kiyomasa Oga 1-5-5 Takatsukadai, Nishi-ku, Kobe-shi, Hyogo Kobe Steel, Ltd. Kobe Research Institute (72) Inventor Motohiro Arai Nishi-ku, Kobe-shi, Hyogo 1-5-5 Takatsukadai Kobe Steel, Ltd.Kobe Research Institute (72) Inventor Hirofumi Okada 14-1, Chofu Minatomachi, Shimonoseki City, Yamaguchi Prefecture Kobe Steel, Ltd.Nagofu Works (72) Inventor Eiji Yoshida 14-1, Chofu Minatomachi, Shimonoseki City, Yamaguchi Prefecture Inside the Kofu Steel Works Chofu Works (72) Inventor Joji Masuda 14-1, Nagafu Minatomachi, Shimonoseki City, Yamaguchi Prefecture Inside the Kofu Steel Works Chofu Works (56) References JP-A-53-80331 (JP, A) JP-A-5-25559 (JP, A) JP-A-60-180998 (JP, U) JP-A-59-34839 (JP, U) (58)査the field (Int.Cl. 7, DB name) B22D 35/00 B22D 11/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 溶解工程における脱酸処理によって、酸
素濃度を10ppm以下にしたCuまたはCu合金の溶
湯を、鋳造工程に移湯するに際して、溶解炉から鋳造機
までの移湯過程中に存在する溶湯落差部のうち、少なく
とも落下高さが20mm以上の溶湯落差部をカバー部材
で覆い、この覆われた領域に不活性ガス気流を形成する
ことを特徴とするCuまたはCu合金の移湯方法。
When a molten metal of Cu or a Cu alloy whose oxygen concentration is reduced to 10 ppm or less by a deoxidizing treatment in a melting step is transferred to a casting step, the molten metal is present in a step of transferring from a melting furnace to a casting machine. A method for transferring Cu or a Cu alloy, comprising: covering at least a molten metal drop portion having a drop height of 20 mm or more with a cover member, and forming an inert gas flow in the covered area.
【請求項2】 前記カバー部材に不活性ガス導入孔およ
び不活性ガス排出孔を設け、前記不活性ガス導入孔から
前記領域の容積の0.2倍/分以上の流量で不活性ガス
を導入すると共に、前記不活性ガス排出孔から排出する
請求項1に記載の移湯方法。
2. An inert gas introduction hole and an inert gas discharge hole are provided in the cover member, and an inert gas is introduced from the inert gas introduction hole at a flow rate of 0.2 times / minute or more of the volume of the region. 2. The hot water transfer method according to claim 1, wherein the hot water is discharged from the inert gas discharge hole.
JP07786295A 1995-04-03 1995-04-03 Method for transferring Cu or Cu alloy Expired - Lifetime JP3178297B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP07786295A JP3178297B2 (en) 1995-04-03 1995-04-03 Method for transferring Cu or Cu alloy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP07786295A JP3178297B2 (en) 1995-04-03 1995-04-03 Method for transferring Cu or Cu alloy

Publications (2)

Publication Number Publication Date
JPH08276260A JPH08276260A (en) 1996-10-22
JP3178297B2 true JP3178297B2 (en) 2001-06-18

Family

ID=13645873

Family Applications (1)

Application Number Title Priority Date Filing Date
JP07786295A Expired - Lifetime JP3178297B2 (en) 1995-04-03 1995-04-03 Method for transferring Cu or Cu alloy

Country Status (1)

Country Link
JP (1) JP3178297B2 (en)

Also Published As

Publication number Publication date
JPH08276260A (en) 1996-10-22

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