JPS6089528A - Treatment of aluminum melt - Google Patents

Treatment of aluminum melt

Info

Publication number
JPS6089528A
JPS6089528A JP19784883A JP19784883A JPS6089528A JP S6089528 A JPS6089528 A JP S6089528A JP 19784883 A JP19784883 A JP 19784883A JP 19784883 A JP19784883 A JP 19784883A JP S6089528 A JPS6089528 A JP S6089528A
Authority
JP
Japan
Prior art keywords
melt
gas
aluminum
molten aluminum
gaseous hydrogen
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.)
Granted
Application number
JP19784883A
Other languages
Japanese (ja)
Other versions
JPS6122012B2 (en
Inventor
Yoshitatsu Otsuka
良達 大塚
Shigemi Tanimoto
谷本 繁美
Kazuo Toyoda
一雄 豊田
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.)
Altemira Co Ltd
Original Assignee
Showa Aluminum Corp
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 Showa Aluminum Corp filed Critical Showa Aluminum Corp
Priority to JP19784883A priority Critical patent/JPS6089528A/en
Priority to DE8484112667T priority patent/DE3480855D1/en
Priority to EP84112667A priority patent/EP0142727B1/en
Priority to US06/663,056 priority patent/US4556419A/en
Priority to AU34545/84A priority patent/AU549799B2/en
Publication of JPS6089528A publication Critical patent/JPS6089528A/en
Publication of JPS6122012B2 publication Critical patent/JPS6122012B2/ja
Granted legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To remove efficiently gaseous hydrogen in an aluminum melt by spraying preliminarily borofluoride salt onto the surface of the aluminum melt and blowing a treating gas in a foaming state into the aluminum melt. CONSTITUTION:While a supply pipe 5 for a treating gas such as N2, Ar, He or the like is rotated by a motor 7, said gas is blown in a foaming state into an aluminum melt 1 put into a treating vessel 2 from a gas releasing member 6 which is attached to the top end of said pipe and vertical grooves 6a to remove gaseous hydrogen and nonmetallic inclusions from the inside of the melt 1. Borofluoride salt such as NaBF4, NH4BF4, etc. is preliminarily blown to the surface of said melt at about >=0.005g/cm<2>, more preferably, 0.01g/cm<2> in this state. The borofluoride salt sprayed by such disposition is decomposed by the heat of the melt 1 and the generated BF3 prevents intrusion of the gaseous hydrogen in the atmosphere above the melt 1 into the melt 1, by which the removing efficiency of the gaseous hydrogen from the melt 1 is improved.

Description

【発明の詳細な説明】 この発明はアルミニウム溶湯の処理方法に関する。[Detailed description of the invention] The present invention relates to a method for treating molten aluminum.

鋳造前のアルミニウム溶湯には、水素ガスなどの有害ガ
スや、アルミニウムおよびマグネシウムの酸化物などの
非金属介在物が含まれている。上記水素ガスおよび非金
属介在物は、得られた鋳塊およびこの鋳塊を拐yr31
どして得られた製品に欠陥を生じさVる原因どなる。そ
のため、水素ガスおよび非金属介在物を除去する必要が
ある。そこで従来、これらを除去する方法として、アル
ミニウム溶湯中に、チッ素ガス、アルゴンガス等の不活
性ガスや塩素ガスを気泡状態で吹込む方法が採用されて
いる。ところが、人気中には水分が含まれているため、
アルミニウム7B 43の表面でアルミニウムと大気中
の水分とが反応しく2A/→−3820−+Al2O3
+3hh)、その結末発生する水素が溶湯中に侵入する
という問題がある。したがって、不活性ガスおよび塩素
ガスを吹込むことによる水素ガス除去9bJ=迭効率が
ぎやめて悪くなる。
Molten aluminum before casting contains harmful gases such as hydrogen gas and nonmetallic inclusions such as oxides of aluminum and magnesium. The hydrogen gas and non-metallic inclusions are removed from the obtained ingot and this ingot for 31 years.
What causes defects in the resulting product? Therefore, it is necessary to remove hydrogen gas and nonmetallic inclusions. Conventionally, as a method for removing these, a method has been adopted in which inert gas such as nitrogen gas or argon gas or chlorine gas is blown into the molten aluminum in the form of bubbles. However, because it contains water,
Aluminum reacts with moisture in the atmosphere on the surface of aluminum 7B 43.2A/→-3820-+Al2O3
+3hh), resulting in the problem that the generated hydrogen enters the molten metal. Therefore, the efficiency of hydrogen gas removal by blowing inert gas and chlorine gas becomes worse.

そこで、上記処理を不活性ガス雰囲気中で行なう方法が
考えられたが、この方法でも雰囲気中の水分量をO,,
5mgz#以下とすることは不可能である。水分量が0
.5111(+/1以下どならなければ、アルミニウム
と反応して生成されてアルミニウム溶湯中に侵入する水
素ガスの量はあまり減らず、不活性ガスajよび塩素ガ
ス吹込みによる水素ガス除去効率はいまだ不十分である
Therefore, a method of performing the above treatment in an inert gas atmosphere was considered, but this method also reduces the amount of moisture in the atmosphere to O,...
It is impossible to reduce the amount to 5 mgz# or less. Water content is 0
.. 5111 (+/1 or less, otherwise the amount of hydrogen gas generated by reacting with aluminum and penetrating into the molten aluminum will not decrease much, and the hydrogen gas removal efficiency by inert gas aj and chlorine gas injection will still be low. Not enough.

この発明は上記実情に鑑みてなされlcものであって、
雰囲気中の水分とアルミニウムどの反応により発生した
水素のアルミニウム溶湯中への侵入を防止することが可
能となり、従来の方法に比べて水素ガス除去効率を大幅
に高めることが可能な処理方法を提供1゛ることを目的
とV−この明細書にa3いて、「アルミニウム」という
語は、純アルミニウムのLSIかにアルミニウム台金も
含む意味で用いられる。
This invention was made in view of the above circumstances, and
Providing a treatment method that can prevent hydrogen generated by the reaction between moisture in the atmosphere and aluminum from penetrating into the molten aluminum, and can significantly increase hydrogen gas removal efficiency compared to conventional methods.1 In this specification, the term "aluminum" is used to include pure aluminum LSIs and aluminum base metals.

この発明によるアルミニウム溶湯の処理方法は、処理槽
内に入れられ1cアルミニウム溶潟中に処理ガスを気泡
状態で吹込んで、アルミニウム溶湯中から水素ガスおよ
び非金属介在物を除去するアルミニウム溶湯の処理方法
において、」上記処理(vllにJ5けるアルミニウム
溶湯の表面に、予め硼弗化塩を散布してd3いてP記処
理を行なうことを特徴とするものである。
A method for treating molten aluminum according to the present invention includes blowing a treatment gas in the form of bubbles into a 1c aluminum molten lag placed in a treatment tank to remove hydrogen gas and nonmetallic inclusions from the molten aluminum. In this process, borofluoride salt is preliminarily sprinkled on the surface of the molten aluminum in J5 and d3 is carried out to perform the process described in P.

上記において、アルミニウム溶湯中に気泡状態で゛吹込
む処理カスとしては、ヂッ索ガス、アルゴンガス、ヘリ
ウムカスおよびこれらの混合カスなどの不活性ガス、な
らびに塩素ガスなど、アルミニウム溶湯中に含j、れる
水素ガスおよび非金属介在物の除去に有効なすべてのガ
スが用いられる。
In the above, the processing scum that is blown into the molten aluminum in the form of bubbles includes inert gases such as gas, argon gas, helium scum, and mixtures thereof, and chlorine gas, which are contained in the molten aluminum. Any gas effective for removing hydrogen gas and non-metallic inclusions may be used.

また、上記に43いて、アルミニウム溶湯の表面に予め
硼弗化塩を散布しておくのはつぎの理由による。すなわ
ら、アルミニウム溶湯の熱により硼弗化塩が分解して1
3F3ガスが発生するが、この13[3ガスが、処1!
l!檜にお(づる溶湯表面よりも上方の“雰囲気中の水
分とアルミニウム溶湯との反応により生じる水素のアル
ミニウム溶湯への浸入をlVjぐ性質を有するからで・
ある。
Further, the reason why borofluoride salt is sprayed on the surface of the molten aluminum in advance in 43 above is as follows. In other words, the borofluoride salt is decomposed by the heat of the molten aluminum, and 1
3F3 gas is generated, but this 13 [3 gas is the place 1!
l! This is because cypress has the property of preventing hydrogen from entering the molten aluminum, which is generated by the reaction between the moisture in the atmosphere above the surface of the molten aluminum and the molten aluminum.
be.

硼弗化塩としては、Na B F、、 、KB F、、
 、L+ o +−t、 、N H/、 l’3 F4
などが用いられる。敗#D ’?lる)lllI弗化塩
の色は、アルミニウム溶湯の表面積にり=i Lで0.
0059/cm2以上とするが好J:シク、どくに0.
01 o /cm2以上がよい。
As borofluoride salts, Na BF, , KB F, ,
, L+ o +-t, , N H/, l'3 F4
etc. are used. Defeat #D'? The color of the fluoride salt depends on the surface area of the molten aluminum = i L and 0.
0059/cm2 or more, but good J: Shiku, Poison 0.
01 o /cm2 or more is preferable.

さらに、アルミニウム溶湯の表面に、硼弗化塩とともに
アルカリ金属また(よアルカリ土類金が一層高まる。ま
た、上記ハロゲン化物の添加用は、アルミニウム溶湯の
表面積I C111′当たり0゜003CI以上どする
のが好ましく、とくに0゜06g以」二どJ−るのがよ
い。
Further, the amount of alkali metal or alkaline earth gold is further increased on the surface of the molten aluminum together with the borofluoride salt.The addition of the above-mentioned halide is carried out at a rate of 0°003 CI or more per surface area of the molten aluminum I C111'. It is preferable that the weight is 0.06 g or more, especially 0.06 g or more.

この発明によるアルミニウム溶湯の処理方法は上述のJ
:うに47.x成されているので、処理槽にお【)る溶
湯よりも上方の雰囲気に含まれる水分とアルミニウムと
が反応して水素が発生したとしても、硼弗化塩が分解し
て発生ずる13F]の働きにJ−りこの水素のアルミニ
ウム溶湯への侵入は防止される。したがって、水素ガス
除去効率は従来の方法に比へて飛躍的に高まる。
The method for treating molten aluminum according to the present invention is described in J.
: Sea urchin 47. 13F, which is generated by the decomposition of the borofluoride salt, even if hydrogen is generated by the reaction between the moisture contained in the atmosphere above the molten metal in the treatment tank and the aluminum. This action prevents hydrogen from entering the molten aluminum. Therefore, the hydrogen gas removal efficiency is dramatically increased compared to conventional methods.

以下この発明の実施例を比較例とともに図面を参照しな
がら説明する。
Examples of the present invention will be described below with reference to the drawings along with comparative examples.

実施例a3よび比較例1〜4 この実施例おJ:び比較例は第1図に示す装置を用いて
行なったもの(゛ある。第1図において、処理すべきア
ルミニウム溶湯(1)は溶湯処理槽(2)内に、溶湯(
1)表面か槽(2)の上端よりも若干上方にくるように
、入れられている。処理槽(2)の上端間口は襟(3)
’r閉塞されている。飴(3)の中央には孔(4)があ
けられており、この孔(4)に上方から処理カス供給管
(5)が挿通されている。処理ガス供給管(5)の下端
部(ま処3!I!槽(2)内の底部近くまで伸びており
、その先端に気泡状処理ガス放出部4.j(6)が取付
(プられている。J、た、処J■(カス供給管(5)は
モーフ(7)により回転させられるようになっている。
Example A3 and Comparative Examples 1 to 4 These Examples and Comparative Examples were carried out using the apparatus shown in Fig. 1. In Fig. 1, the molten aluminum (1) to be treated is In the treatment tank (2), molten metal (
1) It is placed so that the surface is slightly above the top of the tank (2). The upper end of the treatment tank (2) has a collar (3)
'rOccluded. A hole (4) is made in the center of the candy (3), and a treated waste supply pipe (5) is inserted through this hole (4) from above. The lower end of the processing gas supply pipe (5) (extends to near the bottom of the tank (2), and the bubbly processing gas discharge part 4.j (6) is attached to the tip of the pipe (5). (The waste supply pipe (5) can be rotated by the morph (7).

処理ガス放出部(Δ(6〉は円板状で、中央部に処理ガ
ス通過孔(図示略)が形成され、かつ周面に円周方向に
所定間隔をおいて複数の縦tj’j(6a)が形成され
ている。また、M(3)を貴通してN2ノJス供給管(
8)と、排気管(9)とが取付(プられでいる。排気管
(9)は、処理ガス、N2カス、処理ガス供給管く5)
を流れてきた98把ガスは、処理ガス通過孔の下端開口
から放出部材(6)の底面に供給される。づるど、放出
部材(6)の回転により生じる遠心力および縦溝(6a
)の作用によっ−で、小さな処理ガスの気泡が槽く2)
全体にいきわたるように放出される。
The processing gas discharge part (Δ(6〉) is disc-shaped, has a processing gas passage hole (not shown) formed in the center, and has a plurality of longitudinal tj'j ( 6a) is formed.Also, pass through M(3) and connect the N2 supply pipe (
8) and the exhaust pipe (9) are installed (pulled.
The 98-gas that has flowed through is supplied to the bottom surface of the discharge member (6) from the lower end opening of the processing gas passage hole. The centrifugal force generated by the rotation of the discharge member (6) and the longitudinal groove (6a
), small bubbles of process gas are created in the tank 2)
It is released so as to spread throughout the whole body.

このような装置を使用し、溶湯(1)を700〜730
℃に保持し、その表面に硼弗化塩を散布した後、または
散布せずに、処理4?ff (2)におEプる溶湯(1
)の表面J:りも上方の雰囲気中に供給管(8)からN
2ガスを供給しつつ、または供給ぽずに第1表に示づ一
条(4U純度99゜99W[%のアルミニウム溶150
0kgに水素ガス除去処理を施した。処理ガスとしては
Arガスを使用し、これを201/n1inの割合で溶
湯(1)中に吹込lυだ。また、処理ガス供給管(5)
の回転数は650r 、l] 、mとした。各溶湯20
0gを赤熱した鉄製容器に採取し、2TOrrの真空減
圧下で凝固完了までに発生した気泡数を計測した。この
ようにして、水素カス除去処理時間と気泡発生数との関
係を調べた。
Using such a device, melt the molten metal (1) at a temperature of 700 to 730
℃ and after spraying borofluoride salt on its surface or without spraying, treatment 4? ff (2) E-pull molten metal (1
) Surface J: From the supply pipe (8) to the atmosphere above the limo
While supplying two gases or without supplying one gas as shown in Table 1 (4U purity 99°99W [% aluminum molten 150
0 kg was subjected to hydrogen gas removal treatment. Ar gas is used as the processing gas and is blown into the molten metal (1) at a rate of 201/n1 inch. In addition, the processing gas supply pipe (5)
The rotational speed was 650 r, l], m. Each molten metal 20
0 g was collected in a red-hot iron container, and the number of bubbles generated until solidification was completed under a vacuum of 2 TOrr was counted. In this way, the relationship between the hydrogen scum removal treatment time and the number of bubbles generated was investigated.

発生気泡数が少ないほど水素ガス除去;仝2は人さくな
っている。
The fewer the number of bubbles generated, the more hydrogen gas can be removed;

(以下余白) 第 1 表 (以F余白) 実施例および比較例1〜4の結果を第2図にまとめて承
り。
(Hereinafter in the margin) Table 1 (hereinafter in the F margin) The results of Examples and Comparative Examples 1 to 4 are summarized in Fig. 2.

第2図から明らかなように、処し!l槽(2)にa3け
る溶湯(1)表面に硼弗化塩を散布して水素ガスの除去
処理を行4Tつだ場合には、硼弗化塩を散布しないで水
素ガスの除去処理を行な−)た場合に比べて除去効*I
J、飛躍的に向上している。
As is clear from Figure 2, punishment! In case of spraying borofluoride salt on the surface of molten metal (1) in A3 tank (2) to remove hydrogen gas, remove hydrogen gas without spraying borofluoride salt. *I
J. has improved dramatically.

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

第1図はこの発明の方法の実施に用いる装置の垂直断面
図、第2図はこの装置を用いて水素ガス除去処理を行な
った場合の処理時間と気泡発生数との関係を示すグラフ
である。 (1)・・・アルミニウム溶湯、(2)・・・処理槽。 以上 特γF出願人 昭和アルミニウム株式会社第1図 第2図 r 処 理 時 旨 (→
FIG. 1 is a vertical cross-sectional view of an apparatus used to carry out the method of the present invention, and FIG. 2 is a graph showing the relationship between processing time and the number of bubbles generated when hydrogen gas removal is performed using this apparatus. . (1)... Molten aluminum, (2)... Treatment tank. Applicant: Showa Aluminum Co., Ltd. Figure 1 Figure 2 r Processing time (→

Claims (1)

【特許請求の範囲】[Claims] 処理槽内に入れられたアルミニウム溶湯中に処理ガスを
気泡状態で吹込んで、アルミニウム溶湯中から水素カス
および非金属介在物を除去するアルミニウム溶湯の処理
方法において、上記処理槽にd3りるアルミニウム溶湯
の表面に、予め硼弗化塩を散布しておいて上記処理を行
なうことを特徴とづるアルミニウム溶湯の処理方法。
In a method for treating molten aluminum in which hydrogen scum and non-metallic inclusions are removed from the molten aluminum by blowing a treatment gas in the form of bubbles into the molten aluminum placed in the treatment tank, the molten aluminum placed in the treatment tank d3 1. A method for treating molten aluminum, characterized in that the above-mentioned treatment is carried out after spraying borofluoride salt on the surface of the aluminum molten metal.
JP19784883A 1983-10-21 1983-10-21 Treatment of aluminum melt Granted JPS6089528A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP19784883A JPS6089528A (en) 1983-10-21 1983-10-21 Treatment of aluminum melt
DE8484112667T DE3480855D1 (en) 1983-10-21 1984-10-19 METHOD FOR REMOVING HYDROGEN GAS AND NON-METAL IMPURITIES FROM ALUMINUM MELTS.
EP84112667A EP0142727B1 (en) 1983-10-21 1984-10-19 Process for treating molten aluminum to remove hydrogen gas and non-metallic inclusions therefrom
US06/663,056 US4556419A (en) 1983-10-21 1984-10-19 Process for treating molten aluminum to remove hydrogen gas and non-metallic inclusions therefrom
AU34545/84A AU549799B2 (en) 1983-10-21 1984-10-22 Removal of hydrogen and non-metallic inclusions from aluminium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19784883A JPS6089528A (en) 1983-10-21 1983-10-21 Treatment of aluminum melt

Publications (2)

Publication Number Publication Date
JPS6089528A true JPS6089528A (en) 1985-05-20
JPS6122012B2 JPS6122012B2 (en) 1986-05-29

Family

ID=16381341

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19784883A Granted JPS6089528A (en) 1983-10-21 1983-10-21 Treatment of aluminum melt

Country Status (1)

Country Link
JP (1) JPS6089528A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001107154A (en) * 1999-09-03 2001-04-17 Norsk Hydro Asa Device for treating liquid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001107154A (en) * 1999-09-03 2001-04-17 Norsk Hydro Asa Device for treating liquid

Also Published As

Publication number Publication date
JPS6122012B2 (en) 1986-05-29

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