JPS6237329A - Method for refining aluminum and aluminum alloy - Google Patents

Method for refining aluminum and aluminum alloy

Info

Publication number
JPS6237329A
JPS6237329A JP17618785A JP17618785A JPS6237329A JP S6237329 A JPS6237329 A JP S6237329A JP 17618785 A JP17618785 A JP 17618785A JP 17618785 A JP17618785 A JP 17618785A JP S6237329 A JPS6237329 A JP S6237329A
Authority
JP
Japan
Prior art keywords
refining
molten metal
aluminum
refining agent
decomposition
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
JP17618785A
Other languages
Japanese (ja)
Other versions
JPH0774403B2 (en
Inventor
Kenji Osumi
大隅 研治
Toshio Onoe
尾上 俊雄
Haruhiko Toda
戸田 晴彦
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
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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP17618785A priority Critical patent/JPH0774403B2/en
Publication of JPS6237329A publication Critical patent/JPS6237329A/en
Publication of JPH0774403B2 publication Critical patent/JPH0774403B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To facilitate the removal of slag and to reduce erosion by adding a compound which produces gaseous O2 and SO2 by decomposition to a refining agent so as to cover the surface of molten metal with gaseous SO2. CONSTITUTION:About 20wt% compound which produces gaseous O2 and SO2 by decomposition, e.g., potassium sulfate is added to chloride, fluoride or a mixture thereof used as a refining agent during the refining of Al or an Al alloy in a furnace. The surface of the molten metal is covered with generated gaseous SO2 to insulate the molten metal from the atmosphere in the furnace, so the excessive acceleration of reaction is prevented. The irreducible minimum extent of reaction is carried out with oxygen produced from the refining agent.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、アルミニウム及びアルミニウム合金の精練法
に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a method for scouring aluminum and aluminum alloys.

〈従来の技術〉 アルミニウム及びアルミニウム合金の精錬法としては、
例えばC12tなどのハロゲンガス、らしくは少なくと
もハロゲン化合物を含む精錬剤を用いて、脱ガスや脱介
在物処理を行なう方法が一般的である。この場合、精錬
で溶湯表面に浮上した介在物の除滓を容易にするために
、介在物と共存する溶湯の一部を高温で燃焼させて、か
さ比重が小さく、しから溶湯との濡れ性の悪い酸化物等
に変化させることが通常行なわれている。
<Conventional technology> As a refining method for aluminum and aluminum alloys,
For example, it is common to use a halogen gas such as C12t, or a refining agent containing at least a halogen compound, to carry out degassing and removal of inclusions. In this case, in order to easily remove the sludge from the inclusions that have risen to the surface of the molten metal during refining, a portion of the molten metal that coexists with the inclusions is burned at a high temperature, so that the bulk specific gravity is small and the wettability with the molten metal is low. Usually, it is changed to oxides with bad properties.

〈発明が解決しようとする問題点〉 除滓を容易にするために上述のような燃焼処理を行なう
と、溶湯を再生不可能な酸化物等に変化させてしまい、
いわゆる溶損を生じて旧失が大きくなるという問題点が
ある。
<Problems to be solved by the invention> If the above-mentioned combustion treatment is performed to facilitate slag removal, the molten metal will change into oxides etc. that cannot be recycled.
There is a problem that so-called melting loss occurs and the loss of old material becomes large.

本発明はこの点に着目し、除滓性がよく、しかも溶損を
少なくして、除滓性と溶損の両方を満足できるようにす
ることを課題としてなされたものである。
The present invention has focused on this point, and an object of the present invention has been to provide a material that has good sludge removal properties and reduces melting loss, thereby satisfying both the sludge removal properties and melting loss.

く問題点を解決するための手段〉 上記の課題達成のため、本発明のアルミニウム及びアル
ミニウム合金の精錬法では、分解により酸素と二酸化硫
黄ガスを生成する成分を含む精錬剤を用い、溶湯表面を
二酸化硫黄ガスで覆いながら精練するようにしている。
Means for Solving the Problems> In order to achieve the above-mentioned problems, the method for refining aluminum and aluminum alloys of the present invention uses a refining agent containing a component that generates oxygen and sulfur dioxide gas by decomposition, and the surface of the molten metal is heated. The smelting process is done while covering with sulfur dioxide gas.

く作用〉 二酸化硫黄ガスは空気より重く、溶湯の表面を覆って溶
湯と空気との接触を断ち、しかも溶湯とは高温でらほと
んど反応しないため、溶湯と炉内雰囲気中の酸素や窒素
等との反応が妨げられる。
Effect> Sulfur dioxide gas is heavier than air and covers the surface of the molten metal, cutting off contact between the molten metal and the air. Moreover, it hardly reacts with the molten metal even at high temperatures, so it does not interact with the molten metal and oxygen, nitrogen, etc. in the furnace atmosphere. reaction is hindered.

また分解によって生成した酸素は溶湯燃焼用として作用
し、浮上した介在物をかさ比重が小さく、溶湯との濡れ
性の悪い酸化物に変化させると推定される。すなわち、
除滓性の向上と溶損の低減という2つの要求を満足させ
るには、必要最小限の燃焼状態を得るようにすればよい
のであるが、炉内雰囲気中の酸素や窒素によって必要以
上に反応が促進されることを二酸化硫黄ガスが防止し、
精錬剤から生成された酸素によって必要最小限の反応が
行なわれるのである。
It is also presumed that the oxygen generated by the decomposition acts as a molten metal combustion agent and changes the floating inclusions into oxides with low bulk specific gravity and poor wettability with the molten metal. That is,
In order to satisfy the two demands of improving slag removal and reducing melting loss, it is sufficient to obtain the minimum necessary combustion state, but oxygen and nitrogen in the furnace atmosphere may cause reactions to occur more than necessary. sulfur dioxide gas prevents the
The minimum necessary reaction is carried out by the oxygen generated from the refining agent.

〈実施例〉 以下、本発明の実施例について述べる。<Example> Examples of the present invention will be described below.

介在物と共存する溶湯の燃焼を炉内雰囲気中の酸素で行
なうと、反応の制御が困難て溶損が増大するため、本発
明では上述のよ・うに溶湯と炉内雰囲気との接触を断ち
、精錬剤から酸素を供給するようにしている。そこで、
精錬剤の成分として酸素を含む化合物を用いるのであり
、該当する化合物としては炭酸塩、硝酸塩、硫酸塩等が
挙げられろ。
If the molten metal that coexists with inclusions is combusted with oxygen in the furnace atmosphere, it will be difficult to control the reaction and increase melting loss. , oxygen is supplied from a refining agent. Therefore,
A compound containing oxygen is used as a component of the refining agent, and examples of such compounds include carbonates, nitrates, and sulfates.

これらの化合物について検討したところ、炭酸塩は、溶
湯に残留した場合に欠陥の原因となることが発明者らの
実験で判明し、使用を避ける方が望ましいことがわかっ
た。また、硝酸塩は、その化学的性質により配合比によ
っては爆発の危険性があるので、これの使用ら避ける方
がよい。そこで硫酸塩について検討したところ、上記の
ような問題点がなく、新たな技術上の大きな問題点ら生
じなかったので、溶湯燃焼用の酸素供給源として硫酸塩
を用いることが適切であるとの結論が得られた。
After studying these compounds, the inventors found through experiments that carbonates cause defects if they remain in the molten metal, and that it is desirable to avoid their use. Furthermore, due to its chemical properties, nitrates pose a risk of explosion depending on the blending ratio, so it is better to avoid using them. When we investigated sulfates, we found that they did not have the above-mentioned problems and did not pose any new technical problems, so we concluded that it would be appropriate to use sulfates as an oxygen supply source for molten metal combustion. A conclusion has been reached.

更に数種類の硫酸塩についてコスト、反応性等を検討し
たところ、硫酸カリウム(K、So、)が最適であるこ
とが判明したので、具体的にはに、SO4を用いること
とした。検討結果を表1に示す。
Furthermore, after examining the cost, reactivity, etc. of several types of sulfates, it was found that potassium sulfate (K, So,) was the most suitable, so specifically, it was decided to use SO4. The study results are shown in Table 1.

[表!] 次に、本発明では溶湯と炉内雰囲気との接触を断つ手段
として特定のガスで溶湯表面を覆ってシールドしている
。そこで、各種のガスについて、その適性を密度、溶湯
との反応性等について検討したところ、二酸化硫黄(S
Oりが最適であることが判明した。検討結果を表2に示
す。
[table! ] Next, in the present invention, as a means to cut off contact between the molten metal and the atmosphere in the furnace, the surface of the molten metal is covered with a specific gas for shielding. Therefore, we investigated the suitability of various gases in terms of density, reactivity with molten metal, etc., and found that sulfur dioxide (S
It was found that 0 was optimal. The study results are shown in Table 2.

[表2コ 以上の結果、最適と判断されたSO2は、酸素供給源と
して最適と判断されたK 2 S O−の分解で生成さ
せることができる。そこで、通常のアルミニウム及びア
ルミニウム合金の精錬剤として用いられる塩化物、弗化
物あるいはこれらの混合物等にに、SO,を加え、不活
性ガス雰囲気中で900℃まで加熱し、精錬剤の分解反
応を調べた。その結果、S Otガスの発生は、精練剤
の種類に関係なく、一定の温度から生ずることが確認さ
れた。また、表3に示す試験を行ない、除滓性と溶損低
減効果を確認し、K2S0.の効果が認められた。
[As a result of Table 2 and above, SO2 determined to be optimal can be generated by decomposing K 2 SO-, which was determined to be optimal as an oxygen supply source. Therefore, SO was added to chlorides, fluorides, or mixtures thereof, which are commonly used as refining agents for aluminum and aluminum alloys, and heated to 900°C in an inert gas atmosphere to cause the decomposition reaction of the refining agent. Examined. As a result, it was confirmed that S Ot gas was generated at a constant temperature regardless of the type of scouring agent. In addition, we conducted the tests shown in Table 3 to confirm the sludge removal performance and erosion reduction effect, and found that K2S0. The effect of

次に、精錬剤へのに、SO,の配合率と除滓性及び溶損
の関係について、配合率を変えながらその効果を確認し
た。表4に試験条件と結果を示す。
Next, the relationship between the blending ratio of SO in the refining agent, deslag removal performance, and erosion loss was confirmed while changing the blending ratio. Table 4 shows the test conditions and results.

[表4] (a)試験条件 溶湯品種  JIS  5056 精錬剤   KCρ(50vt%)−A(IFバ50−
 awt%)K2SOa(awt%)系 精錬剤使用量溶7A量の0.15wt%精錬方法  N
、ガスによる溶湯への同時吹込み精錬時間   15分 精錬温度   730°C±5°に の結果、本精錬剤系では、K、SO4が2〜20重量%
である場合に除滓性が良好であり、しかも溶損率の低減
に効果があることがわかった。同様に、成分の異なる他
の精錬剤系についても配合率を変えながら試験したとこ
ろ、やはりに!So。
[Table 4] (a) Test conditions Molten metal type JIS 5056 Refining agent KCρ (50vt%)-A (IF Ba 50-
awt%) K2SOa (awt%) Amount of refining agent used: 0.15wt% of 7A amount Refining method N
, Simultaneous injection of gas into the molten metal Refining time: 15 minutes Refining temperature: 730°C ± 5° As a result, in this refining agent system, K and SO4 are 2 to 20% by weight.
It was found that the sludge removal property is good when this is the case, and it is also effective in reducing the erosion rate. Similarly, when we tested other refining agent systems with different ingredients while changing the blending ratio, the results were the same! So.

の配合率が2〜20重量%の場合に除滓性向上と溶損低
減に効果があることが確認された。
It was confirmed that a blending ratio of 2 to 20% by weight was effective in improving sludge removal performance and reducing erosion loss.

次に各種の合金系に対して、普通に用いられる精錬剤系
と、これにに、SO,を配合した場合の結果を表5に示
す。いずれの場合もに!So、を含む場合の方が、除滓
性が向上し且つ溶損が低減しており、効果が確認された
Next, Table 5 shows the results obtained when SO was added to a commonly used refining agent system for various alloy systems. In any case! In the case of containing So, the sludge removal performance was improved and the melting loss was reduced, and the effect was confirmed.

[表5コ (a)試験条件 精練剤へのK t S O−配合率 10wt%精錬条
件 N、ガスによる同時吹込み 温度  730℃±5℃ 溶湯量  15を 精錬剤使用量 1 、5 kg (b)結果 〈発明の効果〉 以上述べたように、本発明は酸素とS O2を生成する
成分を含む精練剤を用いて精錬するものであり、分解に
より生じた酸素が、溶湯表面に存在する介在物と共存す
る溶湯の燃焼に寄与する一方、分解により生じたS O
tガスは燃焼には寄与せず、溶湯表面を覆って炉内雰囲
気からシールドする。
[Table 5 (a) Test conditions K t S O - blending ratio in the scouring agent 10wt% Refining conditions Simultaneous injection of N and gas Temperature 730°C ± 5°C Molten metal amount 15 Amount of refining agent used 1,5 kg ( b) Results <Effects of the Invention> As stated above, the present invention is for refining using a refining agent containing a component that generates oxygen and SO2, and the oxygen generated by decomposition is present on the surface of the molten metal. While contributing to the combustion of the molten metal coexisting with inclusions, the SO generated by decomposition
The t-gas does not contribute to combustion, but covers the molten metal surface and shields it from the furnace atmosphere.

そしてアルミニウム及びアルミニウム合金の溶湯は高温
でもほとんどSO,ガスと反応しないため、最少限の反
応が精錬剤から供給された酸素によって行なわれるもの
と推定される。この結果、反応は過不足なく適正に行な
われ、除滓性の向上と溶損の低減という2つの要求を満
足さ仕ることか可能となるのである。
Since molten aluminum and aluminum alloy hardly reacts with SO and gas even at high temperatures, it is presumed that the minimum reaction is carried out by oxygen supplied from the refining agent. As a result, the reaction can be carried out properly without excess or deficiency, making it possible to satisfy the two demands of improving sludge removal and reducing melting loss.

Claims (2)

【特許請求の範囲】[Claims] (1)分解により酸素と二酸化硫黄ガスを生成する成分
を含む精錬剤を用い、溶湯表面を二酸化硫黄ガスで覆い
ながら精錬することを特徴とするアルミニウム及びアル
ミニウム合金の精錬法。
(1) A method for refining aluminum and aluminum alloys, which is characterized by using a refining agent containing a component that generates oxygen and sulfur dioxide gas by decomposition, and performing refining while covering the surface of the molten metal with sulfur dioxide gas.
(2)特許請求の範囲第1項記載のアルミニウム及びア
ルミニウム合金の精錬法において、分解により酸素と二
酸化硫黄ガスを生成する成分として20重量%以下の硫
酸カリウムを精錬剤に配合して用いるアルミニウム及び
アルミニウム合金の精錬法。
(2) In the method for refining aluminum and aluminum alloys as set forth in claim 1, aluminum and aluminum are used in which 20% by weight or less of potassium sulfate is added to the refining agent as a component that generates oxygen and sulfur dioxide gas by decomposition. Aluminum alloy refining method.
JP17618785A 1985-08-09 1985-08-09 Refining methods for aluminum and aluminum alloys Expired - Lifetime JPH0774403B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17618785A JPH0774403B2 (en) 1985-08-09 1985-08-09 Refining methods for aluminum and aluminum alloys

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17618785A JPH0774403B2 (en) 1985-08-09 1985-08-09 Refining methods for aluminum and aluminum alloys

Publications (2)

Publication Number Publication Date
JPS6237329A true JPS6237329A (en) 1987-02-18
JPH0774403B2 JPH0774403B2 (en) 1995-08-09

Family

ID=16009167

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17618785A Expired - Lifetime JPH0774403B2 (en) 1985-08-09 1985-08-09 Refining methods for aluminum and aluminum alloys

Country Status (1)

Country Link
JP (1) JPH0774403B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02270924A (en) * 1989-04-13 1990-11-06 Kobe Steel Ltd Method for refining molten aluminum and aluminum alloy
US6171362B1 (en) * 1998-12-25 2001-01-09 Kobe Steel, Ltd Method for refining molten aluminum alloy and flux for refining molten aluminum alloy
CN115466871A (en) * 2022-08-25 2022-12-13 江苏立中新材料科技有限公司 Aluminum alloy liquid deslagging, degassing and refining system and method under inert gas protection

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61121409U (en) * 1985-01-16 1986-07-31

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02270924A (en) * 1989-04-13 1990-11-06 Kobe Steel Ltd Method for refining molten aluminum and aluminum alloy
US6171362B1 (en) * 1998-12-25 2001-01-09 Kobe Steel, Ltd Method for refining molten aluminum alloy and flux for refining molten aluminum alloy
CN115466871A (en) * 2022-08-25 2022-12-13 江苏立中新材料科技有限公司 Aluminum alloy liquid deslagging, degassing and refining system and method under inert gas protection
CN115466871B (en) * 2022-08-25 2023-06-23 江苏立中新材料科技有限公司 Aluminum alloy liquid deslagging and degassing refining system and method under inert gas protection

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